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| United States Patent Application |
20090004262
|
| Kind Code
|
A1
|
|
Shaw; Kenneth
;   et al.
|
January 1, 2009
|
Nanoparticulate formulations and methods for the making and use therof
Abstract
The present invention is directed to size-stabilized drug nanoparticulate
compositions and methods of preparation thereof.
| Inventors: |
Shaw; Kenneth; (Weston, CT)
; Zhang; Mingbao; (Stamford, CT)
|
| Correspondence Address:
|
Davidson, Davidson & Kappel, LLC
485 7th Avenue, 14th Floor
New York
NY
10018
US
|
| Assignee: |
Marinus Pharmaceuticals
Branford
CT
|
| Serial No.:
|
998362 |
| Series Code:
|
11
|
| Filed:
|
November 28, 2007 |
| Current U.S. Class: |
424/456; 424/451; 424/464; 424/489; 424/499; 424/501 |
| Class at Publication: |
424/456; 424/489; 424/499; 424/501; 424/464; 424/451 |
| International Class: |
A61K 9/48 20060101 A61K009/48; A61K 9/14 20060101 A61K009/14; A61K 9/20 20060101 A61K009/20 |
Claims
1. Drug complexed particles having a volume weighted median diameter (D50)
from about 50 nm to about 500 nm, each of the particles comprising in
association (i) a drug capable of forming a cyclodextrin inclusion
complex and having an aqueous solubility of less than 1 mg/ml in a pH of
about 7.4, (ii) a surface stabilizer, and (iii) a complexing agent
capable of forming a cyclodextrin inclusion complex when the particles
are cured for at least about 3 days.
2. The drug complexed particles of claim 1, wherein the complexing agent
is included in an amount effective to cause an initial increase in the
size of the particles, wherein the volume weighted median diameter (D50)
of the particles before the initial growth is from about 100 to about 400
nm and the D50 at the end of the curing time is 20% to 300% larger than
the D50 measured before the curing period.
3. The drug complexed particles of claim 1, wherein the surface stabilizer
is at least one non-ionic material selected from the group consisting of
binders, fillers, surfactants/wetting agents; and/or at least one ionic
surface stabilizer.
4. The drug complexed particles of claim 2, wherein the complexing agent
is selected from the group consisting of phenol, parabens, ascorbic acid,
methyl anthranilate, salicylic acid, acetosalicyclic acid, tocopherol,
organic acids, carboxylic acids, aromatic acids, aromatic esters, acid
salts of amino acids, benzaldehyde, cinnimaldehyde, imidazole, menthol,
thiophenol, m-aminobenzoic acid, anthranilic acid, picolinic acids and
alkyl esters thereof, toluidides, sodium benzoate, para-aminobenzoic acid
and esters, sorbic and benzoic acids,
2,6-di-t-butyl-alpha-dimethylamino-p-cresol, t-butylhydroquinone,
di-t-amylhydroquinone, di-t-butylhydroquinone, butylhydroxytoluene (BHT),
butylhydroxyanisole (BHA), pyrocatechol, pyrogallol, esters, isomeric
compounds thereof, pharmaceutically acceptable salts thereof, and
mixtures of any of the foregoing.
5. The drug complexed particles of claim 4, wherein the complexing agent
is selected from the group consisting of methylparaben, propylparaben,
potassium methylparaben, sodium methylparaben, methyl anthranilate,
benzoic acid, sodium benzoate, and any combinations or mixtures thereof.
6. The drug complexed particles of claim 4, which comprise from about 0.1%
to about 8%, w/w of the complexing agent.
7. The drug complexed particles of claim 5, wherein the surface stabilizer
is selected from the group consisting of cellulosics,
polyvinylpyrrolidones, polyethylene glycols, pluronics and any
combinations or mixtures thereof.
8. The drug complexed particles of claim 5, wherein the surface stabilizer
is selected from the group consisting of hydroxypropylmethylcellulose,
polyvinyl alcohol, docusate sodium, sodium lauryl sulfate,
polyvinylpyrrolidone, Plasdone, and mixtures thereof.
9. The drug complexed particles of claim 2, wherein the volume weighted
diameter (D50) of the complexed particles does not change by more than
10% after a time in consecutive measurements separated by about 72 hours.
10. The drug complexed particles of claim 2, wherein the complexed
particles increase in effective particle size from about 0% to about 200%
upon dispersion in simulated gastric or intestinal fluid as compared to
dispersion in water under the same conditions.
11. The drug complexed particles of claim 2, wherein the D50 after the
endpoint is reached is less than about 500 nm.
12. A pharmaceutical composition, comprising the drug complexed particles
of claim 1 together with at least one pharmaceutically acceptable
excipient.
13. The pharmaceutical composition of claim 12, which is in a form of a
solid dosage form.
14. The pharmaceutical composition of claim 12, which is in a form of a
liquid suspension.
15. A method of treatment, comprising administering an effective dose of
the pharmaceutical composition of claim 13 to a human or animal in need
thereof.
16. A method of treatment, comprising administering an effective dose of
the pharmaceutical composition of claim 14 to a human or animal in need
thereof.
17. Size-stabilized drug complexed particles comprising a drug capable of
forming a cyclodextrin inclusion complex and having an aqueous solubility
of less than 1 mg/ml in a pH of about 7.4 in association with effective
amounts of a surface stabilizer and a complexing agent capable of forming
a cyclodextrin inclusion complex, the size-stabilized drug complexed
particles having a volume weighted median diameter (D50) from about 50 nm
to about 500 nm; the drug complexed particles exhibiting an increase in
volume weighted median diameter (D50) of from 0% to not more than about
200% when the formulation is dispersed in simulated gastric fluid (SGF)
or simulated intestinal fluid (SIF) at a concentration of 0.5 to 1 mg
drug/mL and placed in a heated bath at 36.degree. to 38.degree. C. for 1
hour using a Type I or II dissolution apparatus and a stirring rate of 75
RPM, as compared to the D50 of the drug particles when the formulation is
dispersed in distilled water under the same conditions.
18. The size-stabilized drug complexed particles of claim 16, wherein the
surface stabilizer is at least one non-ionic material selected from the
group consisting of binders, fillers, surfactants/wetting agents; and/or
at least one ionic surface stabilizer; and the complexing agent is
selected from the group consisting of phenol, parabens, ascorbic acid,
methyl anthranilate, salicylic acid, acetosalicyclic acid, tocopherol,
organic acids, carboxylic acids, aromatic acids, aromatic esters, acid
salts of amino acids, benzaldehyde, cinnimaldehyde, imidazole, menthol,
thiophenol, m-aminobenzoic acid, anthranilic acid, picolinic acids and
alkyl esters thereof, toluidides, sodium benzoate, para-aminobenzoic acid
and esters, phosphoric acids, sorbic and benzoic acids,
2,6-di-t-butyl-alpha-dimethylamino-p-cresol, t-butylhydroquinone,
di-t-amylhydroquinone, di-t-butylhydroquinone, butylhydroxytoluene (BHT),
butylhydroxyanisole (BHA), pyrocatechol, pyrogallol, esters, isomeric
compounds thereof, pharmaceutically acceptable salts thereof, and
mixtures of any of the foregoing.
19. A pharmaceutical composition, comprising the drug complexed particles
of claim 17 together with at least one pharmaceutically acceptable
excipient.
20. The pharmaceutical composition of claim 19, which is in a form of a
solid dosage form.
21. The pharmaceutical composition of claim 19, which is in a form of a
liquid suspension.
22. The size stabilized drug complexed particles of claim 17, wherein the
complexing agent is selected from the group consisting of methylparaben,
propylparaben, potassium methylparaben, sodium methylparaben, methyl
anthranilate, benzoic acid, sodium benzoate, and any combinations or
mixtures thereof.
23. The size-stabilized drug complexed particles of claim 15, wherein the
complexing agent is methyl anthranilate.
24. A method of treatment, comprising administering an effective dose of
the pharmaceutical composition of claim 20 to a human or animal in need
thereof.
25. A method of treatment, comprising administering an effective dose of
the pharmaceutical composition of claim 21 to a human or animal in need
thereof.
26. The size-stabilized drug complexed particles of claim 17, which
comprise from about 0.1% to about 8%, w/w of the complexing agent.
27. The pharmaceutical composition of claim 20, which is an oral solid
dosage form providing an immediate, delayed, sustained, or pulsatile
release of the drug when orally administered to a human or animal.
28. The pharmaceutical composition of claim 27, wherein the oral solid
dosage form is a tablet or a capsule.
29. The pharmaceutical composition of claim 19, wherein the drug complexed
particles are spray-layered along with effective amounts of a water
soluble spacer and an ionic dispersion modulator onto a plurality of
inert beads.
30. The pharmaceutical composition of claim 29, wherein the ionic
dispersion modulator is in an amount effective to provide a satisfactory
redispersibility of the beads with acceptable particle size and
stability.
31. The composition of claim 29, wherein the ionic dispersion modulator is
an organic or inorganic salt selected from the group consisting of a
magnesium salt, a calcium salt, a lithium salt, a potassium salt, a
sodium salt, a citrate salt, a succinate salt, a fumarate salt, malate
salt, maleate salt, a tartrate salt, a glutarate salt, a lactate salt and
mixtures thereof.
32. A method for preparing stabilized drug particles, comprising:a)
reducing the size of drug particles capable of forming a cyclodextrin
inclusion complex and having an aqueous solubility of less than 1 mg/ml
in a pH of about 7.4 into a size range of about 50 nm to about 200 nm;b)
adding an effective amount of a surface stabilizer to the drug particles
before, during or after reducing the size of the drug particles to form
particles comprising the drug and the surface stabilizer; andc) further
stabilizing the particles of step b) by adding an effective amount of a
complexing agent capable of forming a cyclodextrin inclusion complex to
provide particles that attain a stabilized size such that the volume
weighted median diameter (D50) of the particles is from about 50 nm to
about 500 nm.
33. The method of claim 32, wherein the complexing agent can be added to
the stabilized drug particles of step b) to provide particles that attain
a stabilized size such that the volume weighted median diameter (D50) of
the particles is from about 50 nm to about 500 nm.
34. The method of claim 33, further comprising spraying layering inert
beads with a suspension of the stabilized drug particles together with a
water soluble spacer and an ionic dispersion modulator in an amount
effective to reduce the amount of water soluble spacer needed to
redisperse the spray-layered beads.
35. The method of claim 34, wherein the water soluble spacer comprises
from about 0 to about 60% and the ionic modulator comprises from about 0
to about 40% of the spray-layered particles, by weight stabilized drug
particles.
36. The method of claim 35, wherein the ionic dispersion modulator is
selected from the group consisting of an organic salt, an inorganic salt,
and mixtures thereof.
37. The method of claim 36, wherein the inorganic salts is selected from
the group consisting of a magnesium salt, a calcium salt, a lithium salt,
a potassium salt, a sodium salt and mixtures thereof; and the organic
salt is selected from the group consisting of a citrate salt, a succinate
salt, a fumarate salt, a malate salt, maleate salt, a tartrate salt, a
glutarate salt, a lactate salt and mixtures thereof.
38. A method of treatment, comprising administering the composition of
claim 33 to a human or animal in need thereof.
39. A solid pharmaceutical composition, comprising a plurality of inert
beads spray layered with a coating comprising (a) drug complexed
particles having a volume weighted median diameter (D50) from about 50 nm
to about 500 nm, each of the particles comprising in association (i) a
drug capable of forming a cyclodextrin inclusion complex and having an
aqueous solubility of less than 1 mg/ml in a pH of about 7.4, (ii) a
surface stabilizer, (iii) a complexing agent capable of forming a
cyclodextrin inclusion complex; together with effective amounts of (b) a
water soluble spacer and (c) an ionic dispersion modulator.
40. The pharmaceutical composition, of claim 39, further comprising one or
more pharmaceutically acceptable excipients.
41. The pharmaceutical composition, of claim 40, which is a liquid
suspension of said coated inert beads.
42. The pharmaceutical composition, of claim 40, wherein a therapeutically
effective dose of the coated inert beads are incorporated into a hard
gelatin capsule.
43. The pharmaceutical composition, of claim 42, wherein the coated inert
beads are further over-coated with a coating which imparts a sustained or
delayed release of the drug from the formulation when the formulation is
exposed to simulated gastrointestinal fluid.
44. The pharmaceutical composition, of claim 42, wherein a portion of the
coated inert beads incorporated into the hard gelatin capsule are in
immediate release form and a portion of the inert beads incorporated into
the hard gelatin capsule are in modified release form selected from the
group consisting of sustained release, delayed release and a mixture of
the foregoing, to provide a pulsatile release of drug from the
formulation when the formulation is exposed to simulated gastrointestinal
fluid.
45. An orally ingestible tablet, comprising a compressed mixture of (a)
drug complexed particles having a volume weighted median diameter (D50)
from about 50 nm to about 500 nm, each of the particles comprising in
association (i) a drug capable of forming a cyclodextrin inclusion
complex and having an aqueous solubility of less than 1 mg/ml in a pH of
about 7.4, (ii) a surface stabilizer, (iii) a complexing agent capable of
forming a cyclodextrin inclusion complex; together with effective amounts
of (b) a water soluble spacer and (c) an ionic dispersion modulator; an
inert diluent; and a tableting lubricant.
45. The orally ingestible tablet of claim 45, further comprising one or
more excipients which impart a sustained or delayed or pulsatile release
of the drug from the formulation when the formulation is exposed to
simulated gastrointestinal fluid.
47. A size-stabilized nanoparticulate liquid composition comprising a drug
capable of forming a cyclodextrin inclusion complex and having an aqueous
solubility of less than 1 mg/ml in a pH of about 7.4 in association with
effective amounts of a surface stabilizer and a complexing agent capable
of forming a cyclodextrin inclusion complex, wherein the volume weighted
median diameter (D50) of the size-stabilized particles is from about 50
nm to about 500 nm after curing.
48. The nanoparticulate liquid composition of claim 47, wherein the
composition further contains at least one additional pharmaceutically
acceptable excipient selected from the group consisting of a hydrophilic
polymer, a wetting agent, an ionic dispersion modulator, a water soluble
spacer, and any combinations or mixture thereof.
49. The nanoparticulate liquid composition of claim 47, wherein the liquid
composition is converted to a solid nanoparticulate composition by
removal of solvent.
Description
[0001]This application claims the benefit of U.S. Provisional Patent
Application No. 60/861,616, filed on Nov. 28, 2006, the disclosure of
which is hereby incorporated by reference in its entirety.
FIELD OF THE INVENTION
[0002]Described herein are nanoparticulate formulations of drugs having an
aqueous solubility of less than 1 mg/ml in a pH of about 7.4 which
provide enhanced stability, physical and chemical properties and can
provide enhanced pharmacokinetic properties to achieve an optimal balance
between pharmacodynamic and side effect profiles in mammals, and dosage
forms containing the same, as well as methods of making nanoparticulate
drug formulations and their use in the treatment of various disorders.
BACKGROUND OF THE INVENTION
[0003]It has been very difficult to formulate therapeutically effective
dosage forms specific for drugs having an aqueous solubility of less than
1 mg/ml in a pH of about 7.4, across a broad range of therapeutic agents
(e.g. medroxyprogesterone acetate, carbamazepine, phenyloin, nifedipine
and ganaxolone). Generally, conventional formulations of drugs having an
aqueous solubility less than 1 mg/ml in a pH of about 7.4 demonstrate
variable and low bioavailability and have also shown particularly large
exposure differences when the drug is administered in the fed and fasted
state. Based upon this difficulty, there exists a need in the art for
improved drug formulations and dosage forms for drugs having an aqueous
solubility less than 1 mg/ml in a pH of about 7.4. Herein are described
liquid and solid dosage drug formulations which address this need and
which provide improved pharmacokinetic properties which maintain efficacy
while reducing side effects and enhancing subject compliance.
[0004]Various methods to improve the solubility and bioavailability of
drugs have been used by those skilled in the art. One such method
involves the comminuting in size of the drug particles. Small particles
have more surface area and therefore dissolve into a fixed amount of
media faster. This results in higher oral bioavailability for water
insoluble compounds especially those which have restricted areas of
absorption in the GI tract, have high first pass clearance (liver
metabolism) and have a high dose requirement.
[0005]One way to provide for a small "nano" particle drug formulation is
to form a nanoparticle liquid formulation, e.g., nanosuspension. When
dealing with nanosuspensions, the less water soluble and more lipophilic
the drug, the more difficult it is to obtain a stable small particle
"nanosuspension" in polar solvents like water. Particle growth (Otswald
Ripening) and aggregation must be minimized in nanoparticulate
compositions if the benefit of small particle formulations is to be
realized.
[0006]Preparation of nanosuspensions is known in the art. Most current
commercial technologies involve the use a water based system to generate
small particles (e.g., wet ball milling, precipitation, high pressure
homogenization). Many marketed small particle formulations today are
prepared utilizing wet ball milling techniques. For example, one common
technique entails grinding drug in a milling chamber with grinding media
(beads) to produce small particles. For productivity, those skilled in
the art appreciate that one wants to mill for as short a period of time
needed to make a stable composition and also as concentrated in drug as
possible. Recirculation of a tank of drug suspension through a ball mill
is the most common technique. As the milling is a high energy process, to
avoid contamination from abraded materials (milling chamber and grinding
balls), the shortest milling time possible with the lowest energy is the
most preferred process. As oral nanoparticulate formulations are formed
generally to increase dissolution rates in the gastrointestinal tract,
maintaining a constant particle size until the compound is absorbed is
the key parameter to monitor.
[0007]The preparation of small particle pharmaceutical compositions
(effective particle size (D50) of less than 500 nm) have been described
since 1988 (H. Steffen B T Gattefosse No. 81, 1988 pp. 45-53; U.S. Pat.
No. 4,540,602 (Motoyama, et al.); and U.S. Pat. No. 5,145,684
(Liversidge, et al.)). These submicron (nanoparticulate) compositions all
describe using non-crosslinked excipients associated with the surface of
the small particle to stabilize the composition from significant particle
size growth and/or agglomeration. Generally, surface stabilizers fall
into two categories: non-ionic (also called steric stabilizers or
modifiers) and ionic stabilizers. The most common non-ionic stabilizers
are excipients which are contained in classes known as binders, fillers,
surfactants and wetting agents. Limited examples of non-ionic surface
stabilizers are hydroxypropylmethyl cellulose, polyvinylpyrrolidone,
Plasdone, polyvinyl alcohol, Pluronics, Tweens and Polyethyleneglycols
(PEGs). A subset of surface stabilizers commonly used is ionic in nature.
These ionic surface stabilizers tend to fall into the class of excipients
which are typically used as surfactants and wetting agents. Ionic
stabilizers used in the prior art are typically organic molecules bearing
an ionic bond such that the molecule is essentially fully charged in the
formulation. The two most described ionic surface stabilizers are the
long chain sulfonic acid salts sodium lauryl sulfate and dioctyl sodium
sulfosuccinate (DOSS). Broad ranges for all surface stabilizers have been
claimed in U.S. Pat. No. 5,145,684 (the '684 patent) ranging from 0.1% to
90% by weight of the composition. Typically, one adds 20%-150% (wt % of
drug) of a nonionic surface stabilizer and 0.2%-5% of an ionic surface
stabilizer (wt % of drug) to achieve maximal particle size stabilization
from these surface stabilizers. Since 1988, many papers and patents have
published relating to nanoparticulate compositions and various ways to
optimize the method of manufacture, use and stability of such
compositions.
[0008]In preparing drug nanoparticles via a wet ball milling process as
described in the '684 patent, milling suspensions with drug
concentrations of 5-30% are typically milled with a hard grinding media
in a ball mill to obtain particles with a D50 in the 100-500 nm size
range. The literature teaches that particle size reduction using milling
is conducted at a sufficient speed and time to obtain a desired particle
size. The surface stabilizers are present or added to keep the particle
size constant over a variety of stability indicating measurements as
compared to the particle size (D50) obtained at the end of milling. One
of the major issues in wet ball milling is potential residual metals in
the composition due to extended milling or energy needed to obtain the
desired particle size (Jia, L. Current Nanoscience, 1, pp 237-243
(2005)).
[0009]Enhancing stability has been the focus of much research. Stability
is a broad reference and in the pharmaceutical industry is generally
recognized as testing needed to determine storage stability (the
stability of the formulation under storage over time), purity stability
(the purity profile of the formulation over storage conditions), release
or dispersion stability (the stability of release or disintegration
characteristics for the formulation in water and physiological media).
The physiological media for dispersion stability is dependent on the
route of administration (simulated gastric and/or intestinal fluid for
oral products, saliva for buccal and sub-lingual products, etc). In
general any parameter important to the performance or tolerability of a
formulation must be monitored for stability.
SUMMARY OF THE INVENTION
[0010]Described herein are compositions, pharmaceutical compositions,
methods for treating, methods for formulating, methods for producing,
methods for manufacturing, treatment strategies, pharmacokinetic
strategies using nanoparticulate formulations of drugs having an aqueous
solubility of less than 1 mg/ml in a pH of about 7.4. The drugs that
would benefit from this approach are limited to those that can form a
cyclodextrin complex.
[0011]The inventors have prepared stable submicron drug particles with
particularly advantageous pharmaceutical properties. Stable drug
particles described herein comprise a complex of drug and a complexing
agent. Additional factors that affect stability and particle size are
described herein.
[0012]In certain embodiments, the present invention is directed to drug
complexed particles having a volume weighted median diameter (D50) from
about 50 nm to about 500 nm, each of the particles comprising in
association (i) a drug capable of forming a cyclodextrin inclusion
complex and having an aqueous solubility of less than 1 mg/ml in a pH of
about 7.4, (ii) a surface stabilizer, and (iii) a complexing agent
capable of forming a cyclodextrin inclusion complex when the particles
are cured for at least about 3 days. In certain embodiment, the
complexing agent may be included in an amount effective to cause an
initial increase in the size of the particles, wherein the volume
weighted median diameter (D50) of the particles before the initial growth
is from about 100 to about 400 nm and the D50 at the end of the curing
time is 20% to 300% larger than the D50 measured before the curing
period. For example, in certain embodiments, the complexing agent is
included in an amount from about 0.1% to about 8%, w/w of the
size-stabilized drug particles
[0013]In certain embodiments, the volume weighted diameter (D50) of the
complexed particles does not change by more than 10% after a time in
consecutive measurements separated by about 72 hours.
[0014]In certain embodiments, the complexed particles increase in
effective particle size from about 0% to about 200% upon dispersion in
simulated gastric or intestinal fluid as compared to dispersion in water
under the same conditions.
[0015]In yet another embodiment, the present invention provides for a
pharmaceutical composition comprising the drug complexed particles
described above together with at least one pharmaceutically acceptable
excipient. In certain embodiments, the pharmaceutical composition may be
in the form of a solid dosage form. In other embodiments, the
pharmaceutical composition may be in the form of a liquid dosage form,
e.g., suspension. When incorporated into a pharmaceutical composition
comprising pharmaceutically acceptable excipients, the amount of drug
complexed particles may range from about 1% to about 99%, based on the
weight of the entire composition and the amount of pharmaceutically
acceptable excipient may range from about 1 to about 99% based on the
weight of the total composition.
[0016]In another embodiment, the present invention is directed to
size-stabilized drug complexed particles comprising a drug capable of
forming a cyclodextrin inclusion complex and having an aqueous solubility
of less than 1 mg/ml in a pH of about 7.4 in association with effective
amounts of a surface stabilizer and a complexing agent capable of forming
a cyclodextrin inclusion complex, the size-stabilized drug complexed
particles having a volume weighted median diameter (D50) from about 50 nm
to about 500 nm; the drug complexed particles exhibiting an increase in
volume weighted median diameter (D50) of from 0% to not more than about
200% when the formulation is dispersed in simulated gastric fluid (SGF)
or simulated intestinal fluid (SIF) at a concentration of 0.5 to 1 mg
drug/mL and placed in a heated bath at 36.degree. to 38.degree. C. for 1
hour using a Type I or II dissolution apparatus and a stirring rate of 75
RPM, as compared to the D50 of the drug particles when the formulation is
dispersed in distilled water under the same conditions.
[0017]In certain other embodiments, the present invention is directed to a
solid pharmaceutical formulation, comprising a plurality of inert beads
spray layered with a coating comprising (a) drug complexed particles
having a volume weighted median diameter (D50) from about 50 nm to about
500 nm, each of the particles comprising in association (i) a drug
capable of forming a cyclodextrin inclusion complex and having an aqueous
solubility of less than 1 mg/ml in a pH of about 7.4, (ii) a surface
stabilizer, (iii) a complexing agent capable of forming a cyclodextrin
inclusion complex; together with effective amounts of (b) a water soluble
spacer and (c) an ionic dispersion modulator.
[0018]In another embodiment, the present invention is directed to an
orally ingestible tablet, comprising a compressed mixture of (a) drug
complexed particles having a volume weighted median diameter (D50) from
about 50 nm to about 500 nm, each of the particles comprising in
association (i) a drug capable of forming a cyclodextrin inclusion
complex and having an aqueous solubility of less than 1 mg/ml in a pH of
about 7.4, (ii) a surface stabilizer, (iii) a complexing agent capable of
forming a cyclodextrin inclusion complex; together with effective amounts
of (b) a water soluble spacer and (c) an ionic dispersion modulator; an
inert diluent; and a tableting lubricant.
[0019]In yet another embodiment, the present invention is directed to a
size-stabilized nanoparticulate liquid composition comprising a drug
capable of forming a cyclodextrin inclusion complex and having an aqueous
solubility of less than 1 mg/ml in a pH of about 7.4 in association with
effective amounts of a surface stabilizer and a complexing agent capable
of forming a cyclodextrin inclusion complex, wherein the volume weighted
median diameter (D50) of the size-stabilized particles is from about 50
nm to about 500 nm after curing. The nanoparticulate liquid compositions,
may further contain at least one additional pharmaceutically acceptable
excipient selected from the group consisting of a hydrophilic polymer, a
wetting agent, an ionic dispersion modulator, a water soluble spacer, and
any combinations or mixture thereof.
[0020]In certain embodiments, the nanoparticulate liquid composition is
converted to a solid nanoparticulate composition by removal of solvent
(e.g., via spray drying, spray granulation, spray layering onto inert
cores).
[0021]In yet another embodiment, the present invention is directed to a
method for preparing stabilized drug particles, comprising: a) reducing
the size of drug particles capable of forming a cyclodextrin inclusion
complex and having an aqueous solubility of less than 1 mg/ml in a pH of
about 7.4 into a size range of about 50 nm to about 200 nm; b) adding an
effective amount of a surface stabilizer to the drug particles before,
during or after reducing the size of the drug particles to form particles
comprising the drug and the surface stabilizer; and c) further
stabilizing the particles of step b) by adding an effective amount of a
complexing agent capable of forming a cyclodextrin inclusion complex to
provide particles that attain a stabilized size such that the volume
weighted median diameter (D50) of the particles is from about 50 nm to
about 500 nm.
[0022]In certain embodiments, the size stabilized particles are prepared
by contacting drug particles with a complexing agent such that the size
of the particles exhibits an increase in volume weighted median diameter
of from about 20% to about 300% and an endpoint is reached such that the
particles are size-stabilized. The endpoint can be, e.g., from about 1 to
about 20 days.
[0023]In another embodiment, the present invention is directed to a
suspension of size-stabilized drug complexed particles comprising a drug
capable of forming a cyclodextrin inclusion complex and having an aqueous
solubility of less than 1 mg/ml in a pH of about 7.4 in association with
effective amounts of a surface stabilizer and a complexing agent capable
of forming a cyclodextrin inclusion complex, the size-stabilized drug
complexed particles having a volume weighted median diameter (D50) from
about 50 nm to about 500 nm; the drug complexed particles exhibiting an
increase in volume weighted median diameter (D50) of from 0% to not more
than about 200% when the formulation is dispersed in simulated gastric
fluid (SGF) or simulated intestinal fluid (SIF) at a concentration of 0.5
to 1 mg drug/mL and placed in a vial and heated in a bath at 36.degree.
to 38.degree. C. for 1-3 hours as compared to the D50 of the drug
particles in suspension before dispersion into SGF or SIF.
[0024]In certain embodiments, the size-stabilized drug particles comprise
from about 30 to about 95% drug, from about 3 to about 70% surface
stabilizer, based on the weight of the size-stabilized drug particles,
and from about 0.1% to about 8% complexing agent, based on the weight of
the size-stabilized drug particles.
[0025]In certain embodiments where the complexed size stabilized drug
particles are spray-layered or spray-dried, the particles further
comprise from about 0 to about 40% ionic dispersion modulator and from
about 0% to about 60% water soluble spacer, based on the weight of the
size-stabilized drug particles. In certain embodiments, the amount of
ionic dispersion modulator may range from about 0.1% to 40%. The %
weights are not meant to be limiting.
[0026]The present invention is further directed to methods of preparing
the compositions disclosed herein, including but not limited to, drug
particles, liquid formulations, and solid dosage forms (e.g., immediate
release, sustained release, delayed release and pulsatile release).
[0027]The present invention is also directed to methods of treating
subjects comprising administering to a subject any of the compositions
disclosed herein, including, but not limited to, drug particles, liquid
formulations, and oral solid dosage forms (e.g., immediate release,
sustained release, delayed release and pulsatile release).
[0028]In certain embodiments, the invention is directed to a solid
composition comprising particles comprising a complexed drug; and an
effective amount of an ionic dispersion modulator to reduce agglomeration
and particle size growth of the particles (e.g. upon storage, dispersion
in physiological fluids and water), wherein the volume weighted median
diameter (D50) of the particles is from about 100 nm to about 500 nm.
[0029]In certain embodiments, the invention is directed to a solid
composition comprising particles comprising a complexed nanoparticulate
drug; and an ionic dispersion modulator in an amount of from about 1% to
about 50%, w/w, based on the weight of the size stabilized particles,
wherein the volume weighted median diameter (D50) of the particles
(dispersed in water and/or physiological fluids) is from about 100 nm to
about 500 nm.
[0030]In certain embodiments, the excipient comprises a water soluble
spacer. The water soluble spacer can be a saccharide or an ammonium salt,
a polyethylene glycol or urea that is a solid at temperatures of
50.degree. C. or more. The saccharide can be selected from the group
consisting of fructose, sucrose, glucose, lactose, mannitol and mixtures
thereof. The polyethylene glycol can be selected from PEG 3350, PEG 4000
or PEG 6000.
[0031]In other aspects, the invention is directed to pharmaceutical
particles comprising drug or a pharmaceutically acceptable salt thereof,
the complexed particles being stable (suitable curing time) such that the
volume weighted median diameter (D50) of the particles does not increase
by more than about 50% after 28 days storage at room temperature, the
volume weighted median diameter (D50) of the particles prior to storage
being from about 50 nm to about 500 nm; the particles milled for a
sufficient time to achieve the stability. In other aspects, the volume
weighted median diameter (D50) of the particles does not change by more
than about 25% after 28 days storage at room temperature (25.degree. C.)
conditions, does not change by more than about 15% after 28 days storage
at room temperature, does not change by more than about 10% after 28 days
storage at room temperature (25.degree. C.) and or does not change by
more than about 10% after 4 months storage at 25.degree. C./60% relative
humidity and 40.degree. C./75% relative humidity.
[0032]In another embodiment, the present invention is directed to a
formulation of solid size-stabilized drug complexed particles comprising
a drug capable of forming a cyclodextrin inclusion complex and having an
aqueous solubility of less than 1 mg/ml in a pH of about 7.4 comprising
(a) drug complexed particles having a volume weighted median diameter
(D50) from about 50 nm to about 500 nm, each of the particles comprising
in association (i) a drug capable of forming a cyclodextrin inclusion
complex and having an aqueous solubility of less than 1 mg/ml in a pH of
about 7.4, (ii) a surface stabilizer, (iii) a complexing agent capable of
forming a cyclodextrin inclusion complex, the drug complexed particles
exhibiting an increase in volume weighted median diameter (D50) of from
0% to not more than about 200% when the formulation is dispersed in
simulated gastric fluid (SGF) or simulated intestinal fluid (SIF) at a
concentration of 0.5 to 1 mg drug/mL and placed in a heated bath at
36.degree. to 38.degree. C. for 1-3 hours using a Type I or II
dissolution apparatus and a stirring rate of 75 RPM, as compared to the
D50 of the drug particles when the formulation is dispersed in distilled
water under the same conditions.
[0033]In certain embodiments, the invention is directed to a solid
composition (e.g., a powder, immediate release dosage form, or controlled
release dosage form) comprising size-stabilized drug particles and at
least one pharmaceutically acceptable excipient, the size-stabilized drug
particles exhibiting an increase in volume weighted median diameter (D50)
of from 0% to not more than about 200%, not more than about 150%, not
more than about 100% or not more than about 50%, when the formulation is
dispersed in simulated gastric fluid (SGF) or simulated intestinal fluid
(SIF) at a concentration of 0.5 to 1 mg drug/mL (in any suitable volume,
e.g., 15 mL to 1000 mL) and placed in a heated bath at 360 to 38.degree.
C. without stirring for 1 hour, as compared to the D50 of the drug
particles when the formulation is dispersed in distilled water under the
same conditions, wherein the volume weighted median diameter (D50) of the
drug particles dispersed in distilled water is from about 50 nm to about
1000 nm, from about 100 nm to about 500 nm, or from about 100 nm to about
350 nm. The volume weighted median diameter (D50) of the coated beads
prior to dispersion can be, e.g., from about 0.1 mm to about 5.0 mm. The
solid formulation can be, for example, a powder, a tablet, a capsule,
etc.
[0034]In certain embodiments, the present invention is directed to liquid
pharmaceutical compositions containing size stabilized drug particles
comprising a drug complex exhibiting a D50 after dispersion in SGF or SIF
at 36 to 38.degree. C. for 1-3 hours of not greater than about 500 nm,
and in certain embodiments having a ratio to D50 after such dispersion in
SGF or SIF to the D50 prior to dispersion of less than about 3:1.
[0035]Particle size measurement is generally described and well known to
those skilled in the art. The volume weighted median diameter or D50 is a
commonly accepted measure of particle size. Sometimes one finds loose
aggregates forming upon storage or under physiological fluid testing.
Loose aggregates can generally be broken up via sonication. The formation
of loose aggregates could impact the pharmacokinetic performance
(variability, systemic levels and bioavailability) of a nanoparticulate
formulation. The impact of loose aggregation in a formulation or
physiological fluid must be ascertained on a compound by compound basis
as the performance of a formulation is dependent on a multitude of
variables (dose required, site of absorption, solubility, crystalline
properties and degree of aggregation) of the drug as well as whether the
formulation is a suspension, immediate release or coated solid
formulation protected from gastric fluids. In cases of nanoparticulate
formulations of water insoluble drugs it is obvious that any formulation
that results in less aggregation (loose or otherwise) or particle growth
as measured by an increase in D50 values over time or when exposed to the
physiological media that the drug will be subjected prior or during
absorption is most preferred (more stable). One could theorize, however,
that a nanoparticulate formulation which is formed for a water soluble
compound that is being protected from storage degradation might actually
benefit from aggregates (longer absorption time due to larger effective
particle size). Significant tight aggregation (unreversible) and particle
size growth are obviously undesirable as this would effectively loose the
advantageous increased kinetic dissolution of the drug.
[0036]Hydroxypropylmethyl cellulose, e.g., HPMC-15 and sodium lauryl
sulfate, have also been described as surface stabilizers of drug
nanoparticles in water (H. Steffen B T Gattefosse No. 81, 1988 pp.
45-53).
[0037]Preservatives are also sometimes added to nanosuspensions to protect
the formulation from contamination. For example, Megace ES
Suspension.RTM. (Parr) is preserved with benzoic acid (as sodium benzoate
buffered to pH 4.0 with citric acid and sodium citrate).
[0038]In our U.S. patent application Ser. No. 11/606,222 entitled "Solid
Ganaxolone Formulations and Methods for the Making and Use Thereof" and
U.S. patent application Ser. No. 11/605,700 entitled "Liquid Ganaxolone
Formulations and Methods for the Making and Use Thereof", both of which
were filed on Nov. 28, 2006 and both of which are hereby incorporated by
reference, we disclosed ganaxolone formulations which provide enhanced
stability, physical and chemical properties and can provide enhanced
pharmacokinetic properties to achieve an optimal balance between
pharmacodynamic and side effect profiles in mammals, and dosage forms
containing the same, as well as methods of making ganaxolone formulations
and their use in the treatment of epilepsy-related and other central
nervous system disorders. For example, this enhanced stability was
achieved via the preparation of particles comprising ganaxolone and a
complexing agent, wherein the volume weighted median diameter (D50) of
the particles is from about 50 nm to about 500 nm. The complexing agent
was disclosed as, for example, a paraben, benzoic acid and mixtures
thereof.
CERTAIN DEFINITIONS
[0039]As used herein, the terms "comprising," "including", "containing"
and "such as" are used in their open, non-limiting sense.
[0040]The term "about" is used synonymously with the term "approximately."
As one of ordinary skill in the art would understand, the exact boundary
of "about" will depend on the component of the composition.
Illustratively, the use of the term "about" indicates that values
slightly outside the cited values, i.e., plus or minus 0.1% to 10%, which
are also effective and safe. Thus compositions slightly outside the cited
ranges are also encompassed by the scope of the present claims.
[0041]For purposes of the invention, the term "drug" means any
therapeutically active agent capable of forming a cyclodextrin inclusion
complex in aqueous based solutions/suspensions. In certain embodiments,
such drugs (not as a cyclodextrin inclusion complex) have an aqueous
solubility of less than 1 mg/ml at a pH of about 7.4.
[0042]"Bioavailability" refers to the degree to which a drug becomes
available at the site(s) of action after administration. By way of
illustration, the bioavailability of a drug formulation refers to the
percentage of the weight of drug dosed that is delivered into the general
circulation of the animal or human being studied. The total exposure
(AUC.sub.(0-.infin.)) of a drug when administered intravenously is
usually defined as 100% bioavailable (F %). "Oral bioavailability" refers
to the extent to which drug is absorbed into the general circulation when
the pharmaceutical composition is taken orally as compared to intravenous
injection. The degree and timing in which an active agent becomes
available to the target site(s) after administration is determined by
many factors, including the dosage form and various properties, e.g.,
solubility and dissolution rate of the drug.
[0043]A "blood serum concentration" or "blood plasma concentration" or
"serum or plasma concentration or level", typically measured in mg,
.mu.g, or ng of a drug per ml, dl, or l of serum or plasma absorbed into
the bloodstream after administration. As used herein, measurable plasma
concentrations are typically measured in ng/ml or .mu.g/ml. It is
understood that the plasma concentration of a drug may vary significantly
between subjects, due to variability with respect to metabolism and/or
possible interactions with other therapeutic agents. In accordance with
one aspect of the present invention, the blood plasma concentration of
drug may vary from subject to subject. Likewise, values such as measured
concentration of the active agent in the plasma at the point of maximum
concentration (C.sub.max) or time to reach maximum plasma concentration
(T.sub.max), or total area under the plasma concentration time curve
(AUC.sub.(0-.infin.)) may vary from subject to subject.
[0044]"AUC.sub.(0-.tau.) or "exposure or bioavailability" is the area
under the curve of a graph of the concentration of the active agent
(typically plasma concentration) vs. time (.tau.), measured from time 0
to .tau.. AUC.sub.(0-.tau.) is also used to define the exposure to the
drug over a defined period of time. Due to variability, the amount
necessary to constitute "a therapeutically effective amount" of drug may
vary from subject to subject.
[0045]"Carrier materials" include any commonly used excipients in
pharmaceutics and should be selected on the basis of compatibility with
drug and the release profile properties of the desired dosage form.
[0046]The term "curing" means treating the drug (either before, during or
after particle size reduction) with a complexing agent under suitable
conditions to obtain a size stabilized drug product. In certain
embodiments, a measurement of stability can be via the comparison of the
particle size (e.g., D50) of the uncomplexed drug versus the complexed
drug.
[0047]The term "curing time" means a sufficient time until an endpoint is
reached such that the properties of the (complexed) drug are stabilized.
In certain embodiments, the curing time can be measured as the time until
a size stabilized particle size is reached under a specified test
condition. For example, a suitable curing time may be such a time wherein
the D50 of the (complexed) drug particles do not change or substantially
change after time in consecutive measurements separated by approximately
72 hours, e.g., by more than the accuracy of the measuring
instrument.+-.5%. in 72 hours after the curing period. Preferred curing
times are 1-20 days, 2-15 days or 3-10 days. In other embodiments, a
suitable curing time may be such a time wherein the D50 of the
(complexed) drug particles do not change or substantially change after
time in consecutive measurements over 3 hours at 37.degree. C. in
simulated gastric and/or simulated intestinal fluid.
[0048]The term "complexed" or "complexed nanoparticulate drug" indicates
an association of molecules and/or a particle including drug, a
complexing agent and other components which results in better particle
size stability of drug particles or some other desirable effect. In some
cases, complexing agents initially increase particle size (D50) before
imparting stability or other beneficial attributes to the formulation. In
certain embodiments, complexed drug or complexed nanoparticulate drug
made by adding complexing agents requires a curing time.
[0049]"Complexing agents" are small molecular weight molecules which can
form a cyclodextrin inclusion complex and after suitable curing time
impart additional stability to the drug. Complexing agents include small
compounds under MW 550. Complexing agents include but are not limited to
the group consisting of phenol, parabens, ascorbic acid, methyl
anthranilate, salicylic acid, acetosalicyclic acid, tocopherol, organic
acids, carboxylic acids, aromatic acids, aromatic esters, acid salts of
amino acids, benzaldehyde, cinnimaldehyde, imidazole, menthol,
thiophenol, m-aminobenzoic acid, anthranilic acid, picolinic acids and
alkyl esters thereof, toluidides, sodium benzoate, methylparaben, sodium
methylparaben, para-aminobenzoic acid and esters, sorbic and benzoic
acids, 2,6-di-t-butyl-alpha-dimethylamino-p-cresol, t-butylhydroquinone,
di-t-amylhydroquinone, di-t-butylhydroquinone, butylhydroxytoluene (BHT),
butylhydroxyanisole (BHA), pyrocatechol, pyrogallol, esters, isomeric
compounds thereof, pharmaceutically acceptable salts thereof, and
mixtures of any of the foregoing.
[0050]"Controlled release" or "modified release", consistent with its use
herein, means a dosage form for which the drug release characteristics
versus time and/or conditions at the site of dissolution are chosen to
accomplish therapeutic or convenience objectives not offered by
conventional immediate release dosage forms. Controlled release dosage
forms include sustained release, prolonged release, pulsatile release and
delayed release forms. Controlled release dosage forms can provide
therapeutically effective levels of drug for an extended period of time
and therefore provide a longer therapeutic period relative to immediate
release forms. Addition of a complexing agent can also impart additional
suspension stability during freeze/thaw cycles and boiling if
sterilization is needed.
[0051]"Delayed release", consistent with its use herein, means a dosage
form that releases a portion or all drug at any time other than
immediately after administration and/or at any other location in the
gastrointestinal tract more distal to that which would have been
accomplished by an immediate release dosage form.
[0052]The term "disintegrate" is the dispersion of the dosage form when
contacted with gastrointestinal fluid. "Disintegration agents or
disintegrants" facilitate the breakup or disintegration of a formulation.
Examples of disintegration agents include a starch, e.g., a natural
starch such as corn starch or potato starch, a pregelatinized starch such
as National 1551 or Amijel.RTM., or sodium starch glycolate such as
Promogel.RTM. or Explotab.RTM., a cellulose such as a wood product,
microcrystalline cellulose, e.g., Avicel.RTM., Avicel.RTM. PH101,
Avicel.RTM. PH102, Avicel.RTM. PH105, Elcema.RTM. P100, Emcocel.RTM.,
Vivacel.RTM., Ming Tia.RTM., and Solka-Floc.RTM., methylcellulose,
croscarmellose, or a cross-linked cellulose, such as cross-linked sodium
carboxymethylcellulose (Ac-Di-Sol.RTM.), cross-linked
carboxymethylcellulose, or cross-linked croscarmellose, a cross-linked
starch such as sodium starch glycolate, a cross-linked polymer such as
crosspovidone, a cross-linked polyvinylpyrrolidone, alginate such as
alginic acid or a salt of alginic acid such as sodium alginate, a clay
such as Veegum.RTM. HV (magnesium aluminum silicate), a gum such as agar,
guar, locust bean, Karaya, pectin, or tragacanth, sodium starch glycolate
(Explotab.RTM.), bentonite, a natural sponge, a surfactant, a resin such
as a cation-exchange resin, citrus pulp, sodium lauryl sulfate, sodium
lauryl sulfate in combination starch, and the like.
[0053]"Drug absorption" or "absorption" typically refers to the process of
movement of drug from site of administration of a drug across a barrier
into a blood vessel or the site of action, e.g., a drug moving from the
gastrointestinal tract into the portal vein or lymphatic system.
[0054]"Effective particle size" and "particle size" is interchangeably
used with "D50". By "D50", it is meant that 50% of the particles are
below and 50% of the particles are above a defined measurement. D50 can
be used to describe different parameters (volume, length, number, area .
. . etc). "Effective particle size" or D50 as used herein indicates the
volume-weighted median diameter as measured by a laser/light scattering
method or equivalent, wherein 50% of the particles, by volume, have a
smaller diameter, while 50% by volume have a larger diameter. The volume
weighted D50 also relates to the percentage of weight of the particle
under a certain size. For example a D50 of 500 nm means that 50% of the
particulate mass is less than 500 nm in diameter and 50% of the
particulate mass is greater than 500 nm in diameter. The effective
particle size is measured by conventional particle size measuring
techniques well known to those skilled in the art. Such techniques
include, for example, sedimentation field flow fractionation, photon
correlation spectroscopy, light scattering (e.g., with a Microtrac UPA
150), laser diffraction and disc centrifugation. For the purposes of the
compositions, formulations and methods described herein, effective
particle size is the volume-weighted median diameter as determined using
laser/light scattering instruments and methods, e.g. a Horiba LA-910, or
Horiba LA-950. Similarly, "D90" is the volume-weighted diameter, wherein
90% of the particles, by volume, have a smaller diameter, while 10% by
volume have a larger diameter and "D10" is the volume-weighted diameter,
wherein 10% of the particles, by volume, have a smaller diameter, while
90% by volume have a larger diameter. It is sometimes useful to express
the D50 value after sonication for 1 minute or less using about 40 watts
of sonicating power at room temperature (25.degree. C.).
[0055]An "enteric coating" is a substance that remains substantially
intact in the stomach but dissolves and releases the drug in the small
intestine and/or colon. Generally, the enteric coating comprises a
polymeric material that prevents release in the low pH environment of the
stomach but that ionizes or solubilizes at a higher pH, typically a pH of
5 to 7, but at least above 3.0, more or above 5, or even more
specifically at a pH of about 5.5 to about 7, and thus dissolves
sufficiently in the small intestine and/or colon to release the active
agent therein. In some embodiments, the enteric coatings release greater
than 50% of the drug that is coated in the small intestine. In other
embodiments, the enteric coating provides the release of a substantial
portion (greater than 40%) of the coated drug in the mid-small intestine,
e.g., the jejunum. Additionally, enteric coatings may comprise a
semi-permeable membrane which releases drug slowly in a non pH-dependent
manner.
[0056]The term "grinding media" refers to the material used in milling to
physically reduce the particle size of a composition. For milling
operations, preferred grinding media are spherical balls of yttrium
stabilized zirconium oxide, glass or a plastic resin.
[0057]"Gastrointestinal fluid" is the fluid of the gastrointestinal tract
of a subject or the saliva of a subject or the equivalent thereof. An
"equivalent" of stomach or gastric secretion" is an in vitro fluid having
similar content and/or pH as stomach secretions such as simulated gastric
fluid (SGF) prepared using USP guidance of about 0.1N HCl solution in
water containing about 0.03M NaCl at a pH of around 1.2. In addition, an
"equivalent" of intestinal secretion" is an in vitro fluid having similar
content and/or pH as intestinal secretions such as simulated intestinal
fluid (SIF) prepared using USP guidance is an aqueous phosphate buffer
system at pH of 6.7-6.9.
[0058]"Immediate Release" means a dosage form that releases at least 80%
of drug within 2 hours of administration, more specifically, within 1
hour of addition to a commonly accepted simulated gastric fluid.
Typically an immediate release composition is tested in dissolution
apparatus (Type I or II most common) in an amount considered to be
therapeutic in patients and a volume of SGF of 500-1000 mL.
[0059]"Ionic Dispersion Modulator" is defined as a salt (not a sulfonic
acid), which when added to a complexed small particle composition will
reduce the amount of certain ingredient(s) needed to stabilize solid
dosage forms or blends when dispersed in water, SGF and SIF.
[0060]"Milling chamber void volume" is the open volume in a milling
chamber available to the milling slurry after grinding media has been
added. Milling chamber void volume is related to the amount of grinding
media (volume %) and the volume of open space when the spherical beads
are stacked on one another (grinding media void volume). For 0.2-0.4 mm
spherical milling grinding media, a range of approx. 36-42% of the volume
occupied by the grinding beads is the grinding media void volume. Milling
chamber void volume (mL)=Total milling chamber volume (mL)-volume of
grinding media (mL)+grinding media void volume (mL).
[0061]"Milling residence time" is the time that a particle is present in
the milling chamber over the total time of milling to obtain desired
particles. Milling Residence Time (MRT) is defined as: MRT
(minutes)=Milling chamber void volume (ml).times.total milling time
(minutes)/Milling Slurry Vol. (ml)
[0062]The term "milling slurry" refers to a suspension containing the drug
for particle size reduction and other ingredients to facilitate the
milling process. The composition of the milling slurry is usually not the
final formulation composition.
[0063]The term "milling media" refers to the components of the milling
slurry minus the active pharmaceutical ingredient(s).
[0064]The term "milled slurry" refers the milling slurry after it had been
reduced to a small particle suspension by milling. The most preferred
milling slurries for a liquid dispersion are those that meet particle
size and compositions that can be diluted with water and appropriate
ingredients to obtain the final formulation. For a solid dosage form,
preferred milled slurries are those that can be utilized with minimal
manipulation to yield the final solid dosage form.
[0065]"Pharmacodynamics" refers to the factors which determine the
biologic response observed relative to the concentration of drug at a
site of action.
[0066]"Pharmacokinetics" refers to the factors which determine the
attainment and maintenance of the appropriate concentration of drug at a
site of action.
[0067]"Preservatives" are compounds which inhibit microbial growth and are
typically added to dispersions to prevent microbes from growing.
[0068]A "pulsatile release" dosage form is a dosage form capable of
providing more than one peak blood plasma concentration following a
single administration. A "pulsatile release" formulation can contain a
combination of immediate release, sustained release, and/or delayed
release formulations in the same dosage form.
[0069]"Pharmacokinetic parameters" are parameters which describe the in
vivo characteristics of the drug over time, including, for example plasma
concentration of the drug. Pharmacokinetic parameters include C.sub.max,
T.sub.max, and AUC.sub.0-.tau. (each discussed above).
[0070]"Solubilizers" include compounds such as triacetin, triethylcitrate,
ethyl oleate, ethyl caprylate, sodium lauryl sulfate, sodium doccusate,
vitamin E TPGS, dimethylacetamide, N-methylpyrrolidone,
N-hydroxyethylpyrrolidone, polyvinylpyrrolidone, hydroxypropylmethyl
cellulose, hydroxypropyl cyclodextrins, ethanol, n-butanol, isopropyl
alcohol, cholesterol,
bile salts, polyethylene glycol 200 to 600,
glycofurol, transcutol, propylene glycol, and dimethyl isosorbide,
miglyol, glycerin, glycerol, and the like.
[0071]"Spray Drying" is a process by which a solvent is removed from a
composition yielding a dried form of the ingredients in that composition.
Drying is effected by spraying the composition through a nozzle into a
heated environment containing a vacuum or a flow of air or inert gas.
Spray drying can produce amorphous or crystalline powders of drugs or
granulations, both which can be converted into a solid dosage form by
those skilled in the art.
[0072]"Spray Layering" is a procedure where a solution or suspension
containing ingredients are sprayed through a nozzle into a fluidized bed
containing particles which are coated with a film containing the
composition of the solution or suspension as the solvent is removed by
the flow of a heated gas. Spray layering typically involves coating an
inert core usually comprised of a sugar and starch or cellulosics or
combinations thereof. Such cores are typically 20 to 35 mesh in size.
Spray Layering is used extensively for applying coatings (finish or
enteric) to solid dosage formulations as well as spherical beads
containing a drug for use in a capsule or tablet formulation.
[0073]"Size-stabilized" means the D50 does not substantially change
(greater than 50%) after an initial time is defined (e.g., after an
appropriate curing time) and up to 4 months storage at room temperature
(25.degree. C.). For example, the size stabilized drug particles
described herein in an aqueous dosage form will not show an increase in
effective particle size of greater than 50% over a four month storage
period, and preferably no increase in effective particle size of greater
than 50% over a two year storage period. Similarly, the size-stabilized
drug particles described herein in a liquid or solid form will show an
increase in effective particle size of about 0% to about 200% upon
dispersion in simulated gastric or intestinal fluid as compared to
dispersion in water under the same conditions. In some embodiments, the
formulations described herein does not produce any significant amount of
unidentified drug degradation impurities up to 4 months storage at room
temperature (25.degree. C.) at individual levels of about greater than
0.1% by weight as compared to the impurity levels at the initial time
designation.
[0074]"Stabilizers" include agents which maintain a desirable attribute of
the formulation over a time interval including but not limited to
mechanical, chemical and temperature stressing that can be tested in a
laboratory setting. Such attributes include stable particle size or
homogeneity resulting in concentrations consistent with the labeled
potency and maintaining purity. Some but not all of the attributes are
listed above.
[0075]"Steady state," as used herein, is when the amount of drug
administered is equal to the amount of drug eliminated within one dosing
interval resulting in a plateau or constant plasma drug exposure.
[0076]"Subject" as used herein is any mammal. Subjects include individuals
in need of drug treatment (patients) and individuals not in need of drug
treatment (e.g. normal healthy volunteers. Humans are preferred subjects
and patients.
[0077]"Delayed Release", consistent with its use herein, means a dosage
form that allows at least a one dose reduction in dosing frequency per
day as compared to the drug in conventional form, such as a suspension or
an immediate release solid dosage form.
[0078]A "therapeutically effective amount" or "effective amount" is that
amount of a pharmaceutical agent to achieve a pharmacological effect. The
term "therapeutically effective amount" includes, for example, a
prophylactically effective amount. An "effective amount" of drug is an
amount needed to achieve a desired pharmacologic effect or therapeutic
improvement without undue adverse side effects. The effective amount of a
drug will be selected by those skilled in the art depending on the
particular patient and the disease. It is understood that "an effective
amount" or "a therapeutically effective amount" can vary from subject to
subject, due to variation in metabolism of drug, age, weight, general
condition of the subject, the condition being treated, the severity of
the condition being treated, and the judgment of the prescribing
physician.
[0079]"Treat" or "treatment" refers to any treatment of a disorder or
disease, such as preventing the disorder or disease from occurring in a
subject which may be predisposed to the disorder or disease, but has not
yet been diagnosed as having the disorder or disease; inhibiting the
disorder or disease, e.g., arresting the development of the disorder or
disease, relieving the disorder or disease, causing regression of the
disorder or disease, relieving a condition caused by the disease or
disorder, or reducing the symptoms of the disease or disorder.
BRIEF DESCRIPTION OF THE DRAWINGS
[0080]FIG. 1 is a graph showing the curing curve of sonicated and
unsonicated complexed ganaxolone particles at room temperature
(25.degree. C.). FIG. 1a shows the curing curve of ganaxolone particles
complexed with sodium benzoate at pH 4.0. FIG. 1b shows the curing curve
of ganaxolone particles complexed with parabens.
[0081]FIG. 2 is a graph showing the D50 vs. Time of paraben complexed and
sodium benzoate complexed (at pH 4.0) ganaxolone particles at room
temperature (25.degree. C.).
[0082]FIG. 3 is a graph showing stability plots (D50 vs. Time) of
uncomplexed ganaxolone particles with varying milled residence times.
[0083]FIG. 4 is a graph showing measured D50 values for uncomplexed
ganaxolone particles as a function of milling residence time for a
typical milling run using a Dyno-Mill KDL equipped with four 64 Mm
polyurethane agitator discs.
[0084]FIG. 5 is a graph showing particle size distribution (after 1 minute
low power sonication) of re-suspended solid dosage forms containing
sodium chloride (with and without methylparaben as the complexing agent).
DETAILED DESCRIPTION OF THE INVENTION
[0085]Reference will now be made in detail to embodiments of the
compositions, formulations, and methods disclosed herein. Examples of the
embodiments are illustrated in the following Examples section.
[0086]Unless defined otherwise, all technical and scientific terms used
herein have the same meaning as is commonly understood by one of skill in
the art to which the inventions described herein belong. All patents and
publications referred to herein are incorporated by reference.
[0087]Many drugs are poorly soluble in water and other pharmaceutically
acceptable solvents. As a result of the low aqueous solubility of the
drugs of the present invention, there exists a need in the art for drug
formulations, which provide increased bioavailability and therapeutic
efficacy of the drugs described herein. However, it is known that
increasing the maximal systemic levels (Cmax) of an active agent likewise
results in the possibility of increased side effects.
[0088]The drug formulations described herein can be administered to a
subject by conventional administration routes. Drug oral solid dosage
forms and oral aqueous suspensions are included herein. Immediate,
modified, controlled, and pulsatile release drug dosages forms are
provided herein.
[0089]It is now well-known that drugs which complex with cyclodextrin have
the required shape and size to fit at least partially into the cavity of
the hydrated cyclodextrin molecule; see, for example, Brauns and Muller
European Patent No. 0149197 B1. and Challa et. al.; "Cyclodextrins in
Drug Delivery: An Updated Review". AAPS Pharm Sci Tech. 2005; 06(02):
E329-E357. Such drugs that can form a cyclodextrin inclusion complex are
considered to be within the scope of the invention.
[0090]The drug formulations described herein can comprise drug particles
having a D50 of less than about 500 nm. The starting drug composition can
be predominantly crystalline, predominantly amorphous, or a mixture
thereof. These drug particles can be made by using any method known in
the art for achieving particle sizes of less than 500 nm including, for
example, milling, homogenization, supercritical fluid fracture or
precipitation techniques. Exemplary methods are described in U.S. Pat.
Nos. 4,540,602 and 5,145,684, each of which is specifically incorporated
by reference.
[0091]Methods of making compositions comprising nanoparticles are also
described in U.S. Pat. Nos. 5,518,187; 5,718,388; 5,862,999; 5,665,331;
5,662,883; 5,560,932; 5,543,133; 5,534,270; 5,510,118; 5,470,583 and U.S.
Pub. Appl. 2004/0067251, each of which is specifically incorporated by
reference.
Milling to Obtain Drug Dispersions Comprising Submicron Particles
[0092]In certain embodiments, the drug is milled in order to obtain
submicron particles. The milling process can be a dry process, e.g., a
dry roller milling process, or a wet process, i.e., wet-grinding. In some
embodiments, this invention is practiced in accordance with the
wet-grinding process described in U.S. Pat. Nos. 4,540,602, 5,145,684,
6,976,647 and EPO 498,482, the disclosures of which are hereby
incorporated by reference. Thus, the wet grinding process can be
practiced in conjunction with a liquid dispersion medium and dispersing
or wetting agents such as described in these publications. Useful liquid
dispersion media include water, safflower oil, aqueous salt solutions,
ethanol, n-butanol, hexane, glycol and the like. The dispersing, and/or
wetting agents (alternatively referred to herein and in the prior art as
"surface stabilizers") can be selected from known organic and inorganic
pharmaceutical excipients such as described in U.S. Pat. Nos. 4,540,602
and 5,145,684, and can be present in an amount of 2.0-70%, preferably
3-50%, and more preferably 5-25% by weight based on the total weight of
the drug in the formulation.
[0093]The grinding media for the particle size reduction step can be
selected from rigid media preferably spherical or particulate in shape,
e.g., beads. However, grinding media in the form of other non-spherical
shapes are expected to be useful in the practice of this invention.
[0094]The grinding media preferably can have a mean particle size up to
about 500 microns. In other embodiments of the invention, the grinding
media particles have a mean particle size preferably less than about 500
microns, less than about 100 microns, less than about 75 microns, less
than about 50 microns, less than about 25 microns, less than about 5
microns, less than about 3 mm, less than about 2 mm, less than about 1
mm, less than about 0.25 mm, or less than about 0.05 mm. For fine
grinding, the grinding media particles preferably are from about 0.05 to
about 0.6 mm, more preferably, about 0.1 to about 0.4 mm in size. Smaller
size grinding media will result in smaller size drug particles as
compared to the same conditions using larger sized grinding media.
[0095]In selecting material, grinding media with higher density, e.g.,
glass (2.6 g/cm.sup.3), zirconium silicate (3.7 g/cm.sup.3), and
zirconium oxide (5.4 g/cm.sup.3) and 95% zirconium oxide stabilized with
yttrium, are generally preferred for more efficient milling. Zirconium
oxide, such as 95% Zirconium oxide stabilized with magnesia, zirconium
silicate, and glass grinding media provide particles having levels of
contamination which are believed to be acceptable for the preparation of
therapeutic or diagnostic compositions. However, other media, such as
stainless steel, titania, agate, glass and alumina, are believed to be
useful. In addition, polymeric media having a density typically from
about 1 to about 2 g/cm.sup.3 are also expected to be useful.
[0096]If polymeric grinding media is utilized, then the grinding media can
comprise particles consisting essentially of the polymeric resin.
Alternatively, the grinding media can comprise particles comprising a
core having a coating of the polymeric resin adhered thereon. The
polymeric resin preferably has a density from 0.8 to 3.0 g/cm.sup.3.
Higher density resins are preferred inasmuch as it is believed that these
provide more efficient particle size reduction.
[0097]In general, polymeric resins suitable for use herein are chemically
and physically inert, substantially free of metals, solvent and monomers,
and of sufficient hardness and friability to enable them to avoid being
chipped or crushed during grinding. Suitable polymeric resins include but
are not limited to crosslinked polystyrenes, such as polystyrene
crosslinked with divinylbenzene, styrene copolymers, polycarbonates,
polyacetals, such as Delrin.TM., vinyl chloride polymers and copolymers,
polyurethanes, polyamides, poly(tetrafluoroethylenes), e.g., Teflon.TM.,
and other fluoropolymers, high density polyethylenes, polypropylenes,
cellulose ethers and esters such as cellulose acetate,
polyhydroxymethacrylate, polyhydroxyethyl acrylate, silicone containing
polymers such as polysiloxanes, and the like. The polymeric polymer can
be biodegradable. Exemplary biodegradable polymers include
poly(lactides), poly(glycolide) copolymers of lactides and glycolide,
polyanhydrides, poly(hydroxyethyl methacylate), poly(imino carbonates),
poly(N-acylhydroxyproline)esters, poly(N-palmitoyl hydroxyproline)
esters, ethylene-vinyl acetate copolymers, poly(orthoesters),
poly(caprolactones), and poly(phosphazenes). In the case of biodegradable
polymers, contamination from the media itself advantageously can
metabolize in vivo into biologically acceptable products which can be
eliminated from the body.
[0098]The core material preferably can be selected from materials known to
be useful as grinding media when fabricated as spheres or particles.
Suitable core materials include but are not limited to zirconium oxides
(such as 95% zirconium oxide stabilized with magnesia or yttrium),
zirconium silicate, glass, stainless steel, titania, alumina, ferrite,
and the like. Preferred core materials have a density greater than about
2.5 g/cm.sup.3. The selection of high density core materials is believed
to facilitate efficient particle size reduction.
[0099]Useful thicknesses of the polymeric coating on the core are believed
to range from about 1 to about 500 microns, although other thicknesses
outside this range may be useful in some applications. The thickness of
the polymer coating preferably is less than the diameter of the core.
[0100]The cores can be coated with the polymeric resin by techniques known
in the art. Suitable techniques include spray coating, fluidized bed
coating, and melt coating. Adhesion promoting or tie layers can
optionally be provided to improve the adhesion between the core material
and the resin coating. The adhesion of the polymer coating to the core
material can be enhanced by treating the core material to adhesion
promoting procedures, such as roughening of the core surface, corona
discharge treatment, and the like.
[0101]Grinding can take place in any suitable grinding mill. Suitable
mills include an airjet mill, a roller mill, a ball mill, an attritor
mill, a vibratory mill, a planetary mill, a sand mill and a bead mill. A
high energy media mill is preferred when small particles are desired. The
mill can contain a rotating shaft.
[0102]The preferred proportions of the grinding media, drug, the optional
liquid dispersion medium, and dispersing, wetting or other particle
stabilizing agents present in the grinding vessel can vary within wide
limits and depend on, for example, the size and density of the grinding
media, the type of mill selected, the time of milling, etc. The process
can be carried out in a continuous, batch or semi-batch mode. In high
energy media mills, it can be desirable to fill 80-95% of the volume of
the grinding chamber with grinding media. On the other hand, in roller
mills, it frequently is desirable to leave the grinding vessel up to half
filled with air, the remaining volume comprising the grinding media and
the liquid dispersion media, if present. This permits a cascading effect
within the vessel on the rollers which permits efficient grinding.
However, when foaming is a problem during wet grinding, the vessel can be
completely filled with the liquid dispersion medium or an anti-foaming
agent may be added to the liquid dispersion.
[0103]The attrition time can vary widely and depends primarily upon the
particular drug substance or imaging agent, mechanical means and
residence conditions selected, the initial and desired final particle
size and so forth. For roller mills, processing times from several days
to weeks may be required. On the other hand, milling residence times of
less than about 2 hours are generally required using high energy media
mills.
[0104]After attrition is completed, the grinding media is separated from
the milled drug particulate product (in either a dry or liquid dispersion
form) using conventional separation techniques, such as by filtration,
sieving through a mesh screen, and the like.
[0105]In one aspect of the invention, the grinding media comprises beads
having a size ranging from 0.05-4 mm, preferably 0.1-0.4 mm. For example,
high energy milling of drug with yttrium stabilized zirconium oxide 0.4
mm beads for a milling residence time of 25 minutes to 1.5 hours in
recirculation mode at 1200 to 3000 RPM. In another example, high energy
milling of drug with 0.1 mm zirconium oxide balls for a milling residence
time of 2 hours in batch mode. Additionally, the milling temperature
should not exceed 50.degree. C. as the viscosity of the suspension may
change dramatically. Elevated temperatures also may result in
precipitation of certain polymers in the milling slurry and will increase
wear on the mill seals. If supplies of milled suspension exceeds the void
milling chamber volume then this process will require recycling the
material to a cooled holding tank and re-milling of the material until
the desired particle (D50) size and appropriate properties are achieved
in continuous mode and the mill is also jacketed with cooling. In another
aspect, the mill can be jacketed to help control internal temperatures in
both continuous or batch mode. In our practice, this weight percentage is
based on total weight of the milling slurry. The milling concentration is
from about 10% to about 30% drug by weight vs. the milling slurry weight.
The milling media is defined as the weight of the slurry that is milled
minus the weight of the drug in that slurry. In one embodiment, the
concentration is 25% drug by weight vs. the milling media (weight). In
one embodiment, the milling media contains at least one wetting and/or
dispersing agent (alternatively referred to herein and in the prior art
as "surface stabilizers") to coat the initial drug suspension so a
uniform feed rate may be applied in continuous milling mode. In another
embodiment, batch milling mode is utilized with a milling media
containing at least one agent to adjust viscosity and/or provide a
wetting effect so that the drug is well dispersed amongst the grinding
media.
Microprecipitation to Obtain Drug Dispersions Comprising Nanoparticles
[0106]Drug particles can also be prepared by homogeneous nucleation and
precipitation in the presence of a wetting agent or dispersing agent as
described in U.S. Pat. No. 5,560,932 and U.S. Pat. No. 5,665,331, which
are specifically incorporated by reference. Such drug particles are
storage stable and do not show an appreciable increase in effective
particle size over time. This is a method of preparing stable dispersions
of drug in the presence of one or more dispersing or wetting agents
(alternatively referred to herein and in the prior art as "surface
stabilizers") and one or more colloid stability enhancing surface active
agents. Such a method comprises, for example: (1) dispersing drug in a
suitable liquid media; (2) adding the mixture from step (1) to a mixture
comprising at least on dispersing agent or wetting agent such that at the
appropriate temperature, the drug is dissolved; and (3) precipitating the
formulation from step (2) using an appropriate anti-solvent (e.g.,
water). The method can be followed by removal of any formed salt, if
present, by dialysis or filtration and concentration of the dispersion by
conventional means. In one embodiment, the drug particles are present in
an essentially pure form and dispersed in a suitable liquid dispersion
media. A preferred liquid dispersion medium is water. However, other
liquid media can be used including, for example, aqueous salt solutions,
oils (e.g., safflower, olive or cremephor), and solvents such as ethanol,
t-butanol, hexane, and glycol. The pH of the aqueous dispersion media can
be adjusted by techniques known in the art. In this embodiment, the drug
particles comprise a discrete phase having been admixed with a dispersing
agent or wetting agent. Useful dispersing agents or wetting agents are
experimentally determined, but effectively minimize the difference in
lipophilicity of drug and the dispersion media by inducing a non-covalent
ordered complex between the media, the wetting agent, and drug.
Homogenization to Obtain Drug Dispersions Comprising Nanoparticles
[0107]In yet another embodiment, the drug particles described herein are
produced by high pressure homogenization (see generally U.S. Pat. No.
5,510,118). Such a method comprises dispersing drug particles in a liquid
dispersion medium, followed by subjecting the dispersion to repeated
homogenization to reduce the particle size of the drug to the desired
effective average particle size. The drug particles can be reduced in
size in the presence of at least one or more dispersing agents or wetting
agents. Alternatively, the drug particles can be contacted with one or
more dispersing agents or wetting agents either before or after
attrition. Other compounds, such as a diluent, can be added to the
drug/dispersing agent composition before, during, or after the size
reduction process. In one embodiment, unprocessed drug can then be added
to a liquid medium in which it is essentially insoluble to form a premix.
The concentration of the drug in the liquid medium can vary from about
0.1-60% w/w, and preferably is from 5-30% (w/w). It is preferred, but not
essential, that the dispersing agents or wetting agents be present in the
premix. The concentration of the dispersing agents or wetting agents can
vary from about 0.1 to 90%, and preferably is 1-75%, more preferably
20-60%, by weight based on the total combined weight of the drug and
dispersing agents or wetting agents. The apparent viscosity of the premix
suspension is preferably less than about 1000 centipoise. The premix then
can be transferred to the microfluidizer and circulated continuously
first at low pressures, then at maximum capacity having a fluid pressure
of from about 3,000 to 30,000 psi until the desired particle size
reduction is achieved. The particles must be reduced in size at a
temperature which does not significantly degrade the drug substance or
cause significant particle size growth through solubilization. Next, one
of two methods can be used to collect the slurry and re-pass it in a
microfluidizer. The "discreet pass" method collects every pass through
the microfluidizer until all of the slurry has been passed through before
re-introducing it again to the microfluidizer. This guarantees that every
substance or particle has "seen" the interaction chamber the same amount
of times. The second method re-circulates the slurry by collecting it in
a receiving tank and allowing the entire mixture to randomly mix and pass
through the interaction chamber.
[0108]If some dispersing agents and/or wetting agents, are not present in
the premix, they can be added to the dispersion after attrition in an
amount as described for the premix above. Thereafter, the dispersion can
be mixed, e.g., shaken or stirred.
[0109]The relative amount of drug and dispersing agents and/or wetting
agents (alternatively referred to herein and in the prior art as "surface
stabilizers") can vary widely. The dispersing agents and/or wetting
agents preferably are present in an amount of about 0.1-10 mg per square
meter surface area of drug. The dispersing agents or wetting agents can
be present in an amount of 0.1-90%, preferably 5-50% by weight based on
the total weight of the dry drug particles during the particle size
reduction.
[0110]The resulting drug dispersion is storage stable and consists of the
liquid dispersion medium and the above-described particles. The
dispersion of drug particles can be spray coated onto sugar spheres or
beads or onto a pharmaceutical excipient in a fluid-bed spray coater by
techniques well known in the art.
[0111]The drug particles generated by any of the methods described herein
can be utilized in solid or aqueous liquid dosage formulations, such as
controlled release formulations, pulsatile dosage forms, multiparticulate
dosage forms, solid dose fast melt formulations, lyophilized
formulations, tablets, capsules, aqueous dispersions, or aerosol
formulations.
The Use of Surface Stabilizers
[0112]In certain preferred embodiments, the drug particles are prepared
with the use of one or more materials known in the art as surface
stabilizers or modulators (previously or alternatively referred to herein
or in the art as wetting and/or dispersing agents) which are, e.g.,
adsorbed on the surface of the drug compound. The surface stabilizer(s)
can be contacted with the drug compound either before, during or after
size reduction of the compound. Generally, surface stabilizers fall into
two categories: non-ionic (also called steric stabilizers or modifiers)
and ionic stabilizers. The most common non-ionic stabilizers are
excipients which are contained in classes known as binders, fillers,
surfactants and wetting agents. Limited examples of non-ionic surface
stabilizers are hydroxypropylmethylcellulose, polyvinylpyrrolidone,
Plasdone, polyvinyl alcohol, Pluronics, Tweens and polyethylene glycols
(PEGs). A subset of surface stabilizers commonly used is ionic in nature.
These ionic surface stabilizers tend to fall into the class of excipients
which are typically used as surfactants and wetting agents. Ionic
stabilizers used in the prior art are typically organic molecules bearing
an ionic bond such that the molecule is charged in the formulation. The
two most described ionic surface stabilizers are the long chain sulfonic
acid salts sodium lauryl sulfate and dioctyl sodium sulfosuccinate
(DOSS). Broad ranges for all surface stabilizers have been claimed in
U.S. Pat. No. 5,145,684 (the '684 patent) ranging from 0.1% to 90% by
weight of the composition. Typically, one adds 20%-150% (wt % of drug) of
a nonionic surface stabilizer and 0.2%-5% of an ionic surface stabilizer
(wt % of drug) to achieve maximal particle size stabilization from these
surface stabilizers.
[0113]Conversion of a nanoparticulate composition containing surface
stabilizers is most commonly described via a spray drying, spray
granulation or spray layering process. These procedures are well known in
those skilled in the art. It is also common to add additional excipients
prior to removal of solvent in the nanoparticulate suspension to aid in
the dispersion of the solid composition in medium in which the solid
composition will be exposed (e.g. gastrointestinal fluids) to further
prevent agglomeration and/or particle size growth of the small drug
particles. An example of such an additional excipient is a water soluble
spacer (also referred to as a redispersing agent) which has been
described is sucrose (U.S. Patent Application Publication No.
2004/0214746, the disclosure of which is hereby incorporated by
reference). Other examples of water soluble spacers include sugars,
polyethylene glycols, urea and quarternary ammonium salts.
Obtaining Size Stabilized Particles: Complexing Agents as Particle Growth
Stabilizers
[0114]A concern with the preparation of any small particle suspension is
the stability of the size-reduced (e.g., milled) particles. After size
reduction, the particles after a period of time (e.g., four weeks) may
tend to grow and/or agglomerate and result in increased particle size as
compared to the particles size immediately after size reduction. When
creating small particle formulations (D50 not greater than about 500 nm)
most compositions never stabilize and continue to grow until large
particles (1-30 microns) are realized. The rate at which these particles
grow depends on the composition and the residence time of e.g., milling.
The art around producing small particle compositions of organic molecules
has focused on various methods and compositions to suppress particle
growth or aggregation.
[0115]In contrast, one aspect of the invention is directed to the use of
complexing agent(s) which stabilize the size of the particles. The
addition of such complexing agent(s) initially provide a rapid particle
size growth over a curing period, and then results in size-stabilized
particles which have more desirable attributes than the uncomplexed
particles. Generally, the resultant size-stabilized particles have a D50
value of not greater than about 500 nm (the meaning of size-stabilized is
defined herein at paragraph [0073]). When combined with particles
comprising drugs useful in the present invention (preferably with
effective amounts of a surface stabilizer(s), such complexing agents
provide added stability and superior physical properties such as storage
stability, freeze/thaw stability, heat stability and stability in the
physiological medium (e.g., simulated gastrointestinal fluids) that the
formulation will be exposed to. This enhanced stability allows the small
particle compositions to be exposed to a variety of conditions as
mentioned in the previous sentence and/or to be redispersed while
maintaining a D50 not greater than about 500 nm. Complexing agents also
can minimize the milling time needed to manufacture a stable
nanoparticulate formulation and increase the concentration of drug
content in various formulations.
[0116]The types of complexing agents were not previously identified in the
art as providing such benefits and are small molecular weight molecules
(MW less than 550) which can form a cyclodextrin inclusion complex and
after suitable curing time impart additional stability to the drug.
Complexing agents include but are not limited to aryl or heteroaryl (N,
O, S) aromatic acids and esters and salts thereof. Complexing agents can
be substances containing a phenol moiety, an aromatic ester moiety or an
aromatic acid moiety.
[0117]Examples of complexing agents include but are not limited to phenol,
parabens (e.g., methylparaben, propylparaben, potassium methylparaben,
sodium methylparaben), BHT, sorbic acid, ascorbic acid, methyl
anthranilate, salicylic acid, acetosalicyclic acid, tocopherol, organic
acids, carboxylic acids, aromatic acids, aromatic esters, acid salts of
amino acids, benzaldehyde, cinnimaldehyde, imidazole, menthol,
thiophenol, m-aminobenzoic acid, anthranilic acid, picolinic acids and
alkyl esters thereof, toluidides, sodium benzoate, benzoic acid,
para-aminobenzoic acid and esters, sorbic and benzoic acids,
2,6-di-t-butyl-alpha-dimethylamino-p-cresol, t-butylhydroquinone,
di-t-amylhydroquinone, di-t-butylhydroquinone, butylhydroxytoluene (BHT),
butylhydroxyanisole (BHA), pyrocatechol, pyrogallol, propyl/gallate,
nordihydroguaiaretic acid, esters, and isomeric compounds thereof,
pharmaceutically acceptable salts thereof, mixtures of any of the
foregoing, and the like.
[0118]As demonstrated in the appended Examples, this growth in particle
size is especially observed, e.g., initially after adding methylparaben
with or without propylparaben or benzoic acid/sodium benzoate. A
non-preservative complexing agent providing similar results in the
appended Examples is methyl anthranilate.
[0119]The final storage stable particle size of a nanoparticulate
suspension as measured by volume-weighted-median (D50) is dependent upon
the concentration of the complexing agents and/or milling residence time.
When the concentration of complexing agents was kept constant, the
post-milling growth of particles correlates closely with residence time.
Therefore, certain aspects of the present invention are directed to the
unexpected observation that the residence time that the active agent
particles (e.g., drug particles) are subjected to during the milling
process, has an impact on the variability of the subsequent growth in
particles size after milling. The milling residence time is defined by
the following equation:
Milling Residence Time=(milling chamber void volume/milling slurry
volume).times.milling time (Equation 1).
[0120]Within Equation 1 the void chamber volume is the void space in the
mill chamber that can be occupied by the milling slurry. It is calculated
by estimating the bead void space in the beads (for 0.4 mm
yttrium-stabilized zirconium oxide beads, the bead void space is
approximately 36-40% of the beads volume) and void chamber volume is the
volume of the milling chamber-the volume of the beads+the bead void space
(all in the same volume units). When milling under re-circulating
conditions (passing multiple times through a mill by creating a loop
between a milling slurry in a vessel and the mill, the disclosed
residence times are obtained using flow rates varying from 1/4 of the
estimated void volume/minute to 3 times (3.times.) the estimated void
chamber volume/minute. Ideally flow rates of 0.5.times. void chamber
volume per minute to 1.5.times. void volume per minute are used.
[0121]As demonstrated in the Examples section, it has been observed that
after obtaining a desired particle size, continued milling which does not
significantly reduce the particle size any further, does produce more
growth stable particles as compared to the shorter milling residence time
when measuring storage stability of the formulation. One factor that may
contribute to the growth of the particle size is the association of a
complexing agent with a drug particle. It is also possible that this
complex can further associate with other particle excipients, e.g., a
viscosity enhancing agent or wetting agent (alternatively referred to
herein and in the prior art as "surface stabilizers"). These complexes
which are initially reversible under sonication, increase over the curing
time to become larger, size-stabilized particles. (See FIG. 1). The
curing time is the time needed for the complex to become a
size-stabilized particle. The effect of the milling residence time may
affect the variability of size growth due to that prolonged milling
produces more particles with smoother surfaces that have less area for
contact and are less prone to aggregation. To minimize cost and
contamination of the formulation by abrasion of grinding media and the
portions of the mill in contact with the milling slurry, a preferred
embodiment is shorter and lower energy milling by which a size stabilized
nanoparticulate composition can be formed by adding a complexing agent.
Additional preferred embodiments include nanoparticulate compositions in
which addition of a complexing agent allows for more concentrated drug
compositions.
[0122]Thus, certain embodiments of the present invention provide
pharmaceutical particles comprising complexed drug thereof which exhibit
a stable growth profile over time, i.e., the particles provide a D50
ratio of 1.5:1 or less as compared to D50 after 4 months storage
(25.degree. C.) with the D50 after a suitable curing period. The novel
nature of adding a small molecule complexing agent is seen in some
embodiments where one can reproducibly increase the particle size by
about 20% to 300% within 1-4 weeks curing. After this curing period the
particle size is stable for many months.
[0123]In certain embodiments, the invention is directed to a composition
comprising particles comprising a drug (preferably with a surface
modifier(s) and an effective amount of a complexing agent (added during
or within 24-48 hours after particle size reduction) to stabilize the
particle growth after an initial particle growth and endpoint is reached
(curing time), wherein the volume weighted median diameter (D50) of the
particles before the initial growth is from about 50 to about 200 nm and
the D50 at the end of the curing time is 20% to 300% larger than the D50
measured before the curing period.
[0124]In further embodiments, the particles have a ratio of D50 values
four months storage (25.degree. C.) after curing to of about 1.25:1 or
less; or about 1.15:1 or less.
[0125]In order for the milled drug particles of the present invention to
provide a growth stable profile with drug particles in the 100-500 nm
range (D50), the particles have a preferred milling residence time of at
least 25 minutes if a complexing agent is added. However, these times are
not meant to be limiting. The residence time necessary for obtaining a
growth stable formulation can be ascertained by one of skill in the art,
given the guidance provided by the present disclosure.
[0126]The resultant particles of the milling process disclosed herein can
have a D50 of less than 500 nm, less than 400 nm, less than 300 nm, less
than 200 nm or less than 100 nm. The resultant particles can also have a
D90 of less than 1 micron, less than 500 nm, less than 400 nm, less than
300 nm, less than 200 nm.
[0127]The end product of the milling processes to obtain growth stable
particles can comprise the active agent particles suspended in water
(i.e., a suspension).
[0128]Addition of a complexing agent during or preferably post-milling was
found to improve the physical stability (storage and dispersed in
simulated gastrointestinal fluids) of drug particles formulations (e.g.
liquid suspension and solid formulations). The improvement in physical
stability is believed to be the result of the formation of complex's of
drug particles and the complexing agent which causes an increase in drug
particle size. Without being bound by theory, it is hypothesized that the
increase in drug particle size in complexing agent containing
formulations is achieved through a particle complex forming process. For
example, the complexing agent(s) can act as an aggregating for drug
particles to form drug-aggregates associated with the complexing agent
and possibly other ingredients in the suspension. These aggregates are
relatively weak during the early stages (first 2-3 days) of the complex
formation, e.g. in the case of adding methylparaben or methylparaben and
propylparaben or parabens and benzoic acid/sodium benzoate to ganaxolone.
This is evident as sonication of the formulation in this stage can reduce
the particle size of the complex, apparently due to the loose nature of
the newly-formed complexes. Over a period of time, these loose aggregates
become permanent (irreversible) larger particles. Generally, after no
change in particle size growth is observed over 48 hours the curing
process is complete. When methyl anthranilate is used as a complexing
agent with certain nanoparticulate phenyloin compositions, the curing
time is 5-7 days.
[0129]The initial target size for the drug particles considered desirable
by the inventors was in the range of about 100-200 nm. When milling one
gets a non-linear curve. Initially a large decrease in particle size is
obtained per unit milling time which then decreases so that very little
particle size change with additional milling occurs. Longer milling times
are generally associated with an increase in residual materials (from the
milling chamber lining and balls) in the suspension. On the other hand,
the longer a drug is milled, it has been generally found (e.g., with
ganaxolone), the more stable it is to particle size growth over time.
[0130]The inventors have found that when adding a preservative to a
suspension of drug particles (necessary to preserve the suspension),
e.g., ganaxolone in size range of 100-200 nm manufactured using a surface
stabilizer(s), it was noticed that the drug particles exhibited a rapid
rise in particle size that kept on growing. For example, under high
energy ball milling, if one grinds Ganaxolone to 120-170 nm and then adds
0.1% methylparaben and 0.02% propylparaben (very normal preserving
levels), a rise in particle size to 300 nm was noted, independent of when
the milling process was stopped (i.e., 120 nm sized drug particles grew
to 300 nm; and particles milled for less time and having a particles size
of 170 nm grew to 300 nm) over a 10 day period or so. In view of this
drug particle size growth, the inventors added other preservatives to
milled suspensions not containing parabens. Benzalkonium salts were not
good (flocculation of particles). Addition of sodium benzoate/benzoic
acid showed a slower particle size growth than parabens but also more
than doubled over a few weeks. It was thereafter noted that in the case
where parabens were added to the ganaxolone drug particle suspension, the
particle size of the drug particles stabilized (stopped growing) after a
certain period in time and after following for a few months no further
changes were noted. Despite this fact, it was noted that the methyl and
propyl paraben drug particle suspensions failed when tested for microbial
effectiveness. This was not predicted by the inventors as the levels used
were within 50% of their solubility limit. Thus, the parabens were not
acting as a preservative in the formulation. In fact, a suitable amount
of benzoic acid (added as sodium benzoate) was added to the 300 nm drug
particle suspension in order to pass preservative testing. It is
hypothesized by the inventors that the parabens were tightly bound to the
surface and therefore not able to be an effective preservative. This
hypothesis is provided for possible explanatory purposes only, and is not
meant to be limiting in any way with respect to the appended claims.
[0131]Further studies demonstrated that the addition of methylparaben (and
to a lesser degree, propylparaben) gave ganaxolone suspensions more
stability than without it. It was thereafter found that adding a
non-preservative (methyl anthranilate) caused a rapid rise in particle
size which was then stable. This was the first non-preservative that was
identified as a "complexing" agent. As one follows the ganaxolone
particle size curing period, it was seen that measuring particles size
with and without 60 seconds of sonication showed that initially a loose
association formed (could be reversed partially by sonication) but after
the curing period the particle size of the complexed compositions was
size stable to storage and dispersion in simulated gastrointestinal
fluids. Further evidence to show that methylparaben was acting in a
unique manner in the suspension was seen by filtration. Taking a
ganaxolone suspension (170 nm) containing standard surface stabilizers
but not methylparaben (uncomplexed) could be filtered through a 450 nm
filter and 95% of the particles passed through the filter. After a
paraben curing period significant back pressure was seen in filtration
and only a few percent of the particles filtered through the 450 nm
filter even though at least 60% or more should have. Similar poor
filtration was even seen with 1 and 10 um filters. This result indicated
that the ionic/non-ionic stabilizers with ganaxolone and parabens form a
complicated complex that has a large effective particle size via
filtration (even though laser scattering only shows 300 nm particles
present).
[0132]The manufacture of size-stabilized drug particles can also be
accomplished using a wide range of drugs (as defined herein) and
complexing agents other than the parabens. For example, nanoparticles of
phenyloin (5,5-diphenylhydantoin) have been complexed with methyl
anthranilate to provide initial rapid particle size growth followed by
similarly size-stabilized particles.
[0133]A common property of all complexing agents and drugs which are
capable of forming a complexed, size-stabilized particulate composition
is the ability of these complexing agents and drugs to form a
cyclodextrin inclusion complex. It is now understood that a complexing
agent, as the term is used in the present application, may be defined as
a low molecular weight organic molecule (MW<550) capable of forming a
cyclodextrin inclusion complex.
[0134]Different complexing agents affect the drug (e.g., ganaxolone)
complex formations differently. For example, methylparaben drug complexes
typically take 5 to 7 days to cure while sodium benzoate and/or benzoic
acid-drug aggregates take much longer (up to 3 weeks) to cure, as
illustrated in FIG. 2. FIG. 2 shows the particle size growth plots for
both methylparaben and propylparaben and sodium benzoate (adjusted to pH
4.0) with drug 100 to 200 nm particles. Both formulations contain 5%
drug, 5% HPMC, 1% PVA, 0.1 to 0.2% SLS. The parabens formulation
contained 0.1% methylparaben, 0.02% propylparaben and 0.1% simethicone
while the sodium benzoate formulation contained 0.17% sodium benzoate,
0.13% citric acid and 0.01% sodium citrate (pH 4.0). It has recently been
found that the addition of methyl anthranilate can form a complex which
does not change after sonication after 1 day. In the case of methyl
anthranilate, approximately 0.05% was added to a non-complexed drug
particle suspension at 180 nm and a D50 of 390 nm was seen 72 hours
later. Addition of 0.4% methyl anthranilate increased one ganaxolone
composition from 220 nm to 480 nm over 3 days which was not reversed by
sonication. The 0.4% complexed methyl anthranilate-ganaxolone complex
showed no aggregation in SIF or SGF while the uncomplexed ganaxolone
composition aggregated significantly. Percentages for liquid formulations
are given as wt %/w (weight %/total formulation weight).
[0135]The cured drug-particles appear to have much better physical
stability than drug particles that do not contain the complexing agent.
Once the drug particle complexes are formed, no further substantial
increase in drug particle size is observed. Drug particles of ganaxolone
that were milled for less than 2 hours milling residence time and do not
contain complexing agents continue to increase gradually in size over a
number of months (FIG. 3.).
[0136]Complexing agent concentrations also affect the complex curing
process. Higher concentrations lead to larger particles and faster
curing. For example, two identical drug particle formulations (D50 of 140
nm) with 0.1% and 0.2% methylparaben had D50 values of 190 and 300 nm
respectively after the same curing period.
[0137]Parabens are esters of para-hydroxybenzoic acid. Parabens which can
be utilized in the present invention include methylparaben, ethylparaben,
propylparaben, and butylparaben. Other parabens which can be utilized in
the present invention include isobutylparaben, isopropylparaben,
benzylparaben. Pharmaceutically acceptable salts, e.g., sodium and
potassium salts, can also be utilized in the present invention.
Especially preferred parabens for use in the present invention include
methylparaben and propylparaben and their sodium salts. If the sodium
salts of parabens are utilized an equimolar amount of an organic acid,
e.g., citric acid should be added.
[0138]Typically, milled drug particle suspensions are converted into a
solid dosage form. Governmental drug regulatory agencies such as the FDA,
requires justification of all ingredients and their levels in a
formulation. Therefore, it is quite uncommon for a preservative to be
included in a solid dosage form. With respect to nano-sized dosage forms,
commercialized solid dosage forms prepared from a nanosuspension (e.g.,
TriCor.RTM.), Emmend.RTM.) and Rapamune.RTM.)) do not contain any
preservatives. As shown in the examples, complexing agents impart
significant stability qualities into solid dosage forms.
[0139]The complexing agent can be present in any suitable amount, e.g.,
from about 0.001% to about 5%, from about 0.01% to about 2.5%, from about
0.015% to about 1%, from about 0.1% to about 0.5% or from about 0.02% to
about 0.1%, based on the weight of the milled slurry.
[0140]Certain embodiments of the invention are directed to minimizing
aggregation and/or particle size growth due to the association of the
drug particles and the complexing agent when dispersed in simulated
gastrointestinal fluids. These embodiments are directed to pharmaceutical
particles comprising drug thereof associated with a complexing agent, the
particles exhibiting a ratio of D50 after dispersion in SGF or SIF at
36-38.degree. C. for 1-3 hours to D50 prior to dispersion in SGF or SIF
of less than about 3:1; less than about 2.7:1, less than about 2.5:1,
less than about 2:1, or less than about 1.5:1. In certain embodiments,
the invention is directed to pharmaceutical particles comprising drug
thereof stabilized with a complexing agent, the complexed particles
exhibiting a ratio of D50 after dispersion in SGF or SIF for 1-3 hours to
D50 prior to dispersion of from about 1.5:1 to about 3:1; from about
1.8:1 to about 2.7:1 or about 2:1 to about 1.5:1.
[0141]Certain embodiments of the invention are directed to the "cured"
complexes which exhibit size-stabilized particles. These embodiments are
directed to pharmaceutical particles comprising drug thereof complexed
with a complexing agent, the particles cured for a sufficient time until
an endpoint is reached such that the D50 does not change by more than
about 5% as measured over 3 days after curing. In other embodiments, the
particles are cured for a sufficient time until an endpoint is reached
such that the D50 does not change by more than about 12%, more than about
10%, more than about 8% or more than 5% over 1 month after the curing
period.
[0142]In further embodiments, the particles are cured for a sufficient
time until an endpoint is reached such that the D50 does not change by
more than about 5% (over the instrument's variability at the measure
particle size) after 20 days after curing, 40 days after curing, 60 days
after curing, or 80 days after curing storage conditions of 5.degree. C.
to 25.degree. C. Cured drug particulate complexes are more desirable as
these compositions will provide a more uniform result due to a decreased
change in particle size over time, better thermal stability and less
aggregation in the gastrointestinal tract.
[0143]The endpoint needed to reach size stabilized particles can be
ascertained by one skilled in the art. For example, the endpoint can be
reached in about 5 days to about 25 days; in about 5 days to about 7
days, in about 7 days to about 14 days, in about 14 days to about 21
days, or about 10 days to about 15 days.
[0144]In certain embodiments, the particles have a D50 prior to storage of
less than 350 nm, less than 250 nm or less than 150 nm. In other
embodiments, the particles have a D50 prior to storage of from about 50
nm to about 350 nm, from about 75 nm to about 250 nm or from about 100 nm
to about 150 nm.
[0145]The benefits of having a complexed nanosuspension include but are
not limited to the following: (1) very stable particle size once cured
(e.g., no significant change in particle size after about 2 years); (2)
the non-complexed drug suspensions of similar composition are generally
less stable in simulated gastric and intestinal fluids, e.g., when
incubated at 37.degree. C. for 3 hours; (3) the complexed drug
suspensions can be boiled and frozen without a significant change in
particle size, whereas non-complexed drug suspensions have been found to
double in size (e.g., changing in particle size from 140 nm to 330 nm);
(4) the milling time can be decreased via the use of a complexing agent
to get a storage stable particle size as opposed to obtaining a storage
stable particle size by increasing milling time (also less
contamination). Milling time is also called residence time and is the
time a particle is in the mill when being recirculated through the mill
into a large tank. With complexing agents, milling residence time to
obtain a storage stable drug particle suspension may be, e.g., from about
30 to about 35 minutes versus about 1.5 to 2 hours (which translates to a
3-4 time increase in productivity).
[0146]Complexed drug suspensions comprising drug (e.g., Ganaxolone), HPMC,
SLS, methylparaben, propylparaben, and PVA were found to provide
desirable pharmacokinetic results in animal studies versus uncomplexed
Ganaxolone formulations with D50 values 1/3 that of the complexed
material. Surprisingly, the total exposure (AUC) was slightly higher with
the complexed and higher D50 composition. Previous prior art claims that
smaller particle size result in increased bioavailability which is not
the case with complexed ganaxolone formulations. The smaller uncomplexed
formulation gave higher Cmax values as one would expect with increased
dissolution but not higher bioavailability. Higher Cmax levels without an
increase in bioavailability is an undesirable attribute for some
compounds as higher side effects will be seen without any additional
benefit.
[0147]Formulations containing drug complexes as described above may
provide a more desirable pharmacokinetic performance (e.g., improved
bioavailability, reduction in variability, etc.).
[0148]Milling with Simethicone as an Anti-Foaming Agent
[0149]Foaming during the nanosizing of pharmaceutical products can present
formulation issues and can have negative consequences for particle size
reduction. For example, high levels of foam or air bubbles in the mill
can cause a drastic increase in viscosity rendering the milling process
inoperable. Even a very low level of air presence can dramatically reduce
milling efficiency causing the desired particle size unachievable. This
may be due to the resultant air in the mill cushioning the milling balls
and limiting grinding efficiency. The air also can form a microemulsion
with the milled ingredients which presents many issues with respect to
the delivery of an accurate dose and palatability. Addition of a small
amount of simethicone is a very effective anti-foaming agent which
minimizes milling variability or special handling techniques to avoid the
introduction of air into the milling process.
Drugs
[0150]Suitable drugs which can form a cyclodextrin inclusion complex for
use in the present invention include, but are not limited to,
antineoplastics (anticancer/antitumor agents), sedatives,
antiinflammatory steroids (glucocorticoids such as actometasone,
betamethasone, beclomethasone, fluocinonide, flunisolide, dexamethasone,
cortisone, hydrocortisone, methylprednisolone, mometasone, prednisolone,
prednisone, fluticasone, budesonide, and triamcinolone), tranquilizers,
anticonvulsants, antivirals, antihistaminics (fexofenadine),
vitamins/nutritional factors, emetics (apomorphine), anticoagulants
(dicumarol or coumadin), cardiotonics (including the cardiac glycosides
such as digoxin or digitoxin), diuretics, carbonic anhydrase inhibitors,
non-steroidal analgesic and/or anti-inflammatory agents (NSAID's),
androgens (17-methyltestosterone and testosterone), estrogens, anabolic
agents (fluoxymesterone and methanstenolone), vasodilators, anxiolytics
(e.g, benzodiazepines) antidepressants (sertraline or sulpiride),
antipsyc
hotics (ziprasidone, fluspirilene, pimozide and penfluridole),
hypnotics (etomidate) and/or steroidal hypnotics/anesthetics
(alfaxalone), antifungals, progestins, antiprotozoals, anthelmintics,
anesthetics (lidocaine), vasoconstrictors, hypoglycemic (acetohexamide),
antibacterials/antibiotics, and anti-infectives, platelet inhibitors,
muscle relaxants, antiemetics (dimenhydrinate), radiodiagnostics,
antispasmodics, angiotensin converting enzyme inhibitors, antiarrythmics,
carbonic anhydrase inhibitors, gastrointestinal agents such as loperamide
and cisapride (including H.sub.2-antagonists and other anti-ulcer
agents), antihypertensives especially including those useful as
anti-glaucoma agents, serotonin antagonists, narcotic antagonists,
narcotic agonists, mixed narcotic agonists-antagonists, pharmacologically
active proteins such as peptide hormones, prostaglandins (alprostadil,
prostacyclin or epoprostenol), dopaminergic agents (L-DOPA), mineral
corticoids (desoxycorticosterone), neurosteroids (except for ganaxolone),
enzymes, antibodies and other biologically produced substances,
anti-Parkinsonism/dopamineric agents and drugs for treating Alzheimer's
disease (THA).
[0151]Suitable neurosteroids may include, but are not limited to,
beta-hydroxy-delta 5-compounds, such as pregnenolone (PREG) and
dehydroepiandrosterone (DHEA), their sulfates, and reduced metabolites
such as the tetrahydroderivative of progesterone 3 alpha-hydroxy-5
alpha-pregnane-20-one (3 alpha,5 alpha-THPROG).
[0152]While ganaxolone can indeed form a cyclodextrin inclusion complex,
that drug has been described previously in our U.S. patent application
Ser. Nos. 11/606,222 and 11/605,700, both filed on Nov. 28, 2006, the
disclosures of which are hereby incorporated by reference in their
entirety. However, ganaxolone is therefore excluded from the claims of
the present application.
[0153]Suitable antineoplastics for use in the present invention include,
but are not limited to chlorambucil, lomustine, melphalan, met
hotrexate,
hexamethylmelamine, teniposide, etoposide, semustine (methyl CCNU),
fazarabine (Ara-AC), mercaptopurine, tubulazole, carmofur, carmustine,
amsacrine, doxorubicin, bruceantin, diaziquone, dideminin B, echinomycin
and PCNU.
[0154]Suitable antiinflammatory steroids (glucocorticoids) for use in the
present invention include, but are not limited to actometasone,
betamethasone, beclomethasone, fluocinonide, flunisolide,
fludrocortisone, dexamethasone, cortisone, hydrocortisone,
methylprednisolone, mometasone, prednisolone, prednisone, fluticasone,
budesonide, triamcinolone and any pharmaceutically acceptable salts
thereof. For example, in certain embodiments the glucocorticosteroid is
triamcinolone acetonide.
[0155]Suitable estrogens for use in the present invention include, but are
not limited to, 17.beta.-estradiol, 17.alpha.-ethynylestradiol
(ethinylestradiol), ethynylestradiol 3-methyl ether, estrone, mestranol
and estriol. In certain embodiments, the estrogen is a synthetic
estrogens such as diethylstilbestrol, benzestrol, dienestrol, hexestrol
and the like.
[0156]Suitable progestins for use in the present invention include, but
are not limited to, dimethisterone, norethindrone, norethindrone acetate,
norgestrel, norethynodrel, ethisterone, medroxyprogesterone acetate and
progesterone.
[0157]Suitable immunosuppressive agents for use in the present invention
include, but are not limited to, cyclosporine (also known as cyclosporin
A).
[0158]Suitable anticonvulsants for use in the present invention include,
but are not limited to, phenyloin (5,5-diphenylhydantoin) and
carbamazepine.
[0159]Suitable barbiturates for use in the present invention include, but
are not limited to, pentobarbital, phenobarbital and secobarbital, which
are variously useful as hypnotics, anticonvulsants and sedatives as well.
[0160]Suitable antivirals for use in the present invention include, but
are not limited to, acyclovir, trifluridine, zidovudine, vidarabine and
virazole (also known as ribavirin).
[0161]Suitable vitamins/nutritional for use in the present invention
include, but are not limited to, factors such as retinol (vitamin A),
vitamin A-acetate, cholecalciferol, retinal, retinoic acid (also known as
tretinoin or Retin-A.TM.), isotretinoin, etretinate, acitretin and
.beta.-carotene, collectively referred to herein as retinoids, as well as
other fat-soluble vitamins such as the E, D and K vitamins.
[0162]Beta-blockers suitable for use in the present invention include, but
are not limited to, timolol, atenolol, propranolol, nadolol, carteolol,
carvedilol, celiprolol, esmolol, labetalol, metoprolol, penbutolol,
pindolol and sotalol.
[0163]Diuretics suitable for use in the present invention include, but are
not limited to, chlorthalidone, furosemide, spironolactone, and other
sulfonamide-type and/or aldosterone antagonist-type diuretics.
[0164]Angiotensin converting enzyme inhibitors (ACE inhibitors) suitable
for use in the present invention, include but are not limited to,
enalaprilic acid (the diacid, sometimes called `enalaprilate`), the ethyl
ester of enalaprilic acid (sometimes called enalapril), captopril,
lisinopril and SCH-33861.
[0165]Suitable non-steroidal analgesics and/or anti-inflammatory agents
for use in the present invention include, but are not limited to,
aspirin, ibuprofen, indomethacin, piroxicam, sulindac and flurbiprofen.
[0166]Antibacterials/antibiotics, anti-infectives and/or
antifungal/antiprotozoal agents suitable for use in the present invention
include, but are not limited to, ampicillin, penicillin G; tetracycline,
chlortetracycline, oxytetracycline, demeclocycline, methacycline,
doxycycline, minocycline, erythromycin, josamycin, rosamycin, tylosin,
troleandomycin and spiramycin, benzalkonium chloride, cetylpyridinium
chloride, chlorhexidine, econazole, clotrimazole, oxiconazole,
bifonazole, metronidazole (metronidazole benzoate), fenticonazole,
miconazole, sulconazole, tioconazole, isoconazole, butoconazole,
ketoconazole, doconazole, parconazole, orconazole, valconazole and
lombazole, terconazole, itraconazole, omidazole, camidazole,
ipronidazole, tinidazole and nimorazole, and flubendazole.
[0167]Suitable vasodilators include, but are not limited, to coronary
vasodilators such as nitroglycerin, flunarizine, lidoflazine and
mioflazine.
[0168]Carbonic anhydrase inhibitors suitable for use in the present
invention include, but are not limited to, acetazolamide, chlorzolamide,
ethoxzolamine, methazolamide, L-671,152 and MK-927.
[0169]H.sub.2-antagonists suitable for use in the present invention
include, but are not limited to, famotidine, burimamide, metiamide,
cimetidine and oxmetidine.
[0170]Antihistaminics suitable for use in the present invention include,
but are not limited to, astemizole, levocabastine, flunarizine, oxatomide
and cinnarizine.
[0171]Anthelmintic agents suitable for use in the present invention
include, but are not limited to, thiabendazole, oxibendazole,
cambendazole, fenbendazole, flubendazole, albendazole and oxfendazole.
[0172]Serotonin antagonists suitable for use in the present invention
include, but are not limited to, ketanserin, ritanserin, altanserin, and
mianserin.
[0173]Benzodiazepines suitable for use in the present invention, include
but are not limited to, chlordiazepoxide, diazepam, medazepam, oxazepam,
lorazepam, flunitrazepam, estazolam, flurazepam, loprazolam,
lormetazepam, nitrazepam, quazepam, temazepam and triazolam.
[0174]In certain embodiments, the drug formulations comprise a
non-amorphous form of drug comprising drug particles having an effective
particle size by weight of less than about 500 nm. In other embodiments,
the drug particles have an effective particle size by weight of less than
about 400 nm, an effective particle size by weight of less than about 300
nm, an effective particle size by weight of less than about 200 nm, or an
effective particle size by weight of less than about 100 nm when measured
by the above techniques. In yet another embodiment, the drug particles
have a particle size distribution wherein the drug particles have an
effective particle size by weight of less than about 400 nm and wherein
the standard deviation of the particle size distribution is less than
about 100 nm.
[0175]In other embodiments, the drug particles by weight have a particle
size 500 nm, i.e., less than about 500 nm, less than about 400 nm, less
than about 300 nm, less than about 200 nm, or less than about 100 nm with
less than at least 20%, at least about 15% or at least about 10% of the
total particles having a particle size greater than 1 micron.
[0176]In one embodiment, the drug particles have a particle size of around
300 nm with a distribution wherein 90% of the particles by weight have an
effective particle size by weight between about 100 nm and 800 nm. In
another embodiment, the drug particles have a particle size or around 100
nm and a distribution wherein 90% of the particles by weight have an
effective particle size by weight between about 50 nm and 250 nm.
[0177]In other embodiments, the drug compositions described herein
comprise size stabilized drug particles having a particle size by weight
of less than 500 nm formulated with drug particles having a particle size
by weight of greater than 500 nm. In such embodiments, the formulations
have a particle size distribution wherein about 10% to about 100% of the
drug particles by weight are between about 100 nm and about 300 nm, about
0% to about 90% of the drug particles by weight are between about 300 nm
and about 600 nm, and about 0% to about 30% of the drug particles by
weight are greater than about 600 nm. In one embodiment, the formulation
has a particle size distribution wherein about 20% of the drug particles
by weight are between about 100 nm and about 300 nm, about 40% of the
drug particles by weight are between about 300 nm and about 600 nm, and
about 30% of the drug particles by weight are greater than about 600 nm.
In still another embodiment, the formulation has a particle size
distribution wherein about 30% of the drug particles by weight are
between about 100 nm and about 300 nm, about 40% of the drug particles by
weight are between about 300 nm and about 600 nm, and about 30% of the
drug particles by weight are greater than about 600 nm. In yet another
embodiment, the formulation has a particle size distribution wherein
about 50% of the drug particles by weight are between about 100 nm and
about 300 nm, about 40% of the drug particles by weight are between about
300 nm and about 800 nm, and about 10% of the drug particles by weight
are greater than about 800 nm.
[0178]The drug particles generated by the methods described herein can be
utilized in solid or aqueous liquid dosage formulations, such as
controlled release formulations, solid dose fast melt formulations,
lyophilized formulations, tablets, capsules, aqueous dispersions, or
aerosol formulations.
Dosage Forms
[0179]The drug compositions described herein can be formulated for
administration to a subject via any conventional means including, but not
limited to, oral, parenteral (e.g., intravenous, subcutaneous, or
intramuscular), buccal, intranasal or transdermal administration routes.
[0180]Moreover, the pharmaceutical drug compositions described herein can
be formulated into any suitable dosage form, including but not limited
to, aqueous oral dispersions, aqueous oral suspensions, solid dosage
forms including oral solid dosage forms, aerosols, controlled release
formulations, fast melt formulations, effervescent formulations,
self-emulsifying dispersions, solid solutions, liposomal dispersions,
lyophilized formulations, tablets, capsules, pills, powders, delayed
release formulations, immediate release formulations, modified release
formulations, extended release formulations, pulsatile release
formulations, multiparticulate formulations, and mixed immediate release
and controlled release formulations. In some embodiments, drug
formulations provide a therapeutically effective amount of drug over an
interval of about 30 minutes to about 8 hours after administration,
enabling, for example, once-a-day, twice-a-day (b.i.d.), or three times a
day (t.i.d.) administration if desired. In one embodiment, the drug
particles are formulated into a controlled release or pulsatile solid
dosage form for b.i.d. administration. In other embodiments, the drug
particles are dispersed in an aqueous dispersion for b.i.d.
administration. Generally speaking, one will desire to administer an
amount of drug needed to elicit a therapeutic effect in the minimal
number of dosings per unit time.
[0181]In certain embodiments of the invention, the stabilized drug
particle suspensions are converting to a solid form. There are generally
four ways to accomplish this: spray drying; spray layering onto a core
(fluidized bed); spray granulation (fluidized bed); or adding more
excipients and performing a spheronization extrusion.
[0182]The inventors have found that several issues may arise when removing
water from the stabilized drug particle suspension in order to prepare a
solid dosage form. For example, there can be particle aggregation in the
solid state or particle aggregation (increase in particle size) may occur
when the solidified drug particles are re-dispersed into a biological
medium.
Spray-Layering
[0183]In a spray layering manufacture, the cores (e.g., inert beads) are
sprayed with droplets of the drug particle suspension, e.g., in a Wurster
column. The entire particle should preferably be coated evenly. Then, the
water in the suspension has to evaporate before the beads circulated
through the Wurster column again. It has been found that uncomplexed drug
particles can be spray layered but are generally not stable in SGF and
SIF. The complexed (cured particles with a complexing agent) are
generally more stable; nevertheless, additional agents are typically
added to make spray layering (coating) work give optimal results.
[0184]In general, it is considered by those skilled in the art that it is
preferable to make the slurry to be sprayed as concentrated in drug
particles as possible. Spray drying manufacture allows the drug
concentration to approach 80% or higher. In spray layering manufacture,
however, it has been typical to add a lot of sucrose into the drug
particle dispersion, which is believed to act as a water soluble spacer
separating the drug particles from agglomeration during spraying and
re-dispersion. The inventors have found that spray layered ganaxolone
drug-complex beads prepared by spray layering without sucrose had good
water redispersion, but aggregated more substantially in SGF and SIF. The
inventors then determined that adding a small amount of a salt such as
sodium chloride dramatically reduced the amount of sucrose needed to help
redisperse solid nanoparticulate composition with good particle size and
stability. For example, a 1.5 weight % (as compared to drug) addition of
NaCl reduced the amount of sucrose (water soluble spacer 20-fold (from
100% weight of drug to 5% weight of drug) to achieve minimal aggregation
when dispersed in SGF. This dramatic effect has been able to provide a
greater concentration of drug, thereby allowing more drug to be delivered
in one capsule unit. As the stability effects are seen primarily in SGF
and SIF, the salt is referred to as an "ionic dispersion modulator" as it
seems to have its best effects when redispersing into an ionic medium.
[0185]In certain embodiments, the excipient comprises an ionic dispersion
modulator. The ionic dispersion modulator can be a salt such as an
organic or inorganic salt. In certain preferred embodiments, the ionic
dispersion modulator is an inorganic salt. Suitable inorganic salts
include, but are not limited to a magnesium salt, a calcium salt, a
lithium salt, a potassium salt, a sodium salt and mixtures thereof. In
certain preferred embodiments, the inorganic salt is sodium chloride. In
other preferred embodiments, the salt is an organic salt. Suitable
organic salts include, but are not limited to a citrate salt, a succinate
salt, a fumarate salt, a malate salt, maleate salt, a tartrate salt, a
glutarate salt, a lactate salt and mixtures thereof. In yet other
embodiments, the ionic dispersion modulator includes one or more of both
an inorganic and organic salt.
[0186]The amount of ionic dispersion modulator included in a
spray-layering process should be an amount effective to provide a
satisfactory redispersibility of the beads with acceptable particle size
and stability, without causing the mixture to become a semi-solid. Such
an amount typically may comprise from about 0.2% to about 5% as compared
to weight of drug in the formulation.
Oral Solid Dosage Forms
[0187]In some embodiments, the solid dosage forms of the present invention
may be in the form of a tablet (including a suspension tablet, a
fast-melt tablet, a bite-disintegration tablet, a rapid-disintegration
tablet, an effervescent tablet, or a caplet), a pill, a powder (including
a sterile packaged powder, a dispensable powder, or an effervescent
powder), a capsule (including both soft or hard capsules, e.g., capsules
made from animal-derived gelatin or plant-derived HPMC, or "sprinkle
capsules"), solid dispersion, solid solution, bioerodible dosage form,
controlled release formulations, pulsatile release dosage forms,
multiparticulate dosage forms, pellets, granules, or an aerosol. In other
embodiments, the pharmaceutical formulation is in the form of a powder.
In still other embodiments, the pharmaceutical formulation is in the form
of a tablet, including but not limited to, a fast-melt tablet.
Additionally, pharmaceutical formulations of the present invention may be
administered as a single capsule or in multiple capsule dosage form. In
some embodiments, the pharmaceutical formulation is administered in two,
or three, or four, capsules or tablets.
[0188]In some embodiments, solid dosage forms, e.g., tablets, effervescent
tablets, and capsules, are prepared by mixing drug particles with one or
more pharmaceutical excipients to form a bulk blend composition. When
referring to these bulk blend compositions as homogeneous, it is meant
that the drug particles are dispersed evenly throughout the composition
so that the composition may be readily subdivided into equally effective
unit dosage forms, such as tablets, pills, and capsules. The individual
unit dosages may also comprise film coatings, which disintegrate upon
oral ingestion or upon contact with diluents. These drug formulations can
be manufactured by conventional pharmaceutical techniques.
[0189]In certain aspects, the solid formulation is in the form of a tablet
or capsule containing the size stabilized complexed drug particles and at
least one surface stabilizer, the size stable drug particles exhibiting
an increase in volume weighted median diameter (D50) of from 0% to not
more than about 200%, not more than about 150%, not more than about 100%,
or not more than about 50%, when the tablets or capsules are dispersed in
SGF or SIF (in any suitable volume, e.g., 15 mL to 1000 mL) at a
concentration of 0.5 to 1 mg drug/mL at 36.degree. to 38.degree. C. using
a Type I or II dissolution apparatus and a stirring rate of 75 RPM for 1
hour, as compared to the D50 of the drug particles when the tablets or
capsules are dispersed in distilled water under the same conditions,
wherein the volume weighted median diameter (D50) of the drug particles
when the tablets or capsules are dispersed in distilled water is from
about 50 nm to about 1000 nm, from about 100 nm to about 500 nm, or from
about 100 nm to about 350 nm.
[0190]In other aspects, the invention is directed to a solid formulation
(e.g., a powder, immediate release dosage form, or controlled release
dosage form) comprising size stabilized drug particles and at least one
pharmaceutically acceptable excipient, the size stabilized drug particles
exhibiting a volume weighted median diameter (D50) of less than about 500
nm when the formulation is dispersed in simulated gastric fluid (SGF) for
one hour followed by simulated intestinal fluid (SIF) for three
additional hours, at a concentration of 0.5 to 1 mg drug/mL (in any
suitable volume, e.g., 15 mL to 1000 mL) at a temperature of 36.degree.
to 38.degree. C.
[0191]In still other aspects, the solid formulation is a tablet or capsule
containing the stabilized drug particles and at least one excipient, the
stable drug particles exhibiting a volume weighted median diameter (D50)
of less than about 500 nm when the tablets or capsules are dispersed in
simulated gastric fluid (SGF) for one hour followed by simulated
intestinal fluid (SIF) for three additional hours, at a concentration of
0.5 to 1 mg drug/mL (in any suitable volume, e.g., 15 mL to 1000 mL) at a
temperature of 36.degree. to 38.degree. C. using a Type I or II
dissolution apparatus and a stirring rate of 75 RPM.
Preparation of Solid Dosage Forms
[0192]Conventional pharmaceutical techniques for preparation of solid
dosage forms include, e.g., one or a combination of methods: (1) dry
mixing, (2) direct compression, (3) milling, (4) dry or non-aqueous
granulation, (5) wet granulation, or (6) fusion. See, e.g., Lachman et
al., The Theory and Practice of Industrial Pharmacy (1986). Other methods
include, e.g., spray drying, pan coating, melt granulation, granulation,
fluidized bed spray drying or coating (e.g., wurster coating), tangential
coating, top spraying, tableting, extruding and the like.
Formulation Components
[0193]The pharmaceutical solid dosage forms described herein can comprise
the drug compositions described herein and one or more pharmaceutically
acceptable additives such as a compatible carrier, binder, complexing
agent, ionic dispersion modulator, filling agent, suspending agent,
flavoring agent, sweetening agent, disintegrating agent, dispersing
agent, surfactant, lubricant, colorant, diluent, solubilizer, moistening
agent, plasticizer, stabilizer, penetration enhancer, wetting agent,
anti-foaming agent, antioxidant, preservative, or one or more combination
thereof. In still other aspects, using standard coating procedures, such
as those described in Remington's Pharmaceutical Sciences, 20th Edition
(2000), a film coating is provided around the drug formulation. In one
embodiment, some or all of the drug particles are coated. In another
embodiment, some or all of the drug particles are microencapsulated. In
yet another embodiment, some or all of the drug is amorphous material
coated and/or microencapsulated with inert excipients. In still another
embodiment, the drug particles not microencapsulated and are uncoated.
[0194]Suitable carriers for use in the solid dosage forms described herein
include, but are not limited to, acacia, gelatin, colloidal silicon
dioxide, calcium glycerophosphate, calcium lactate, maltodextrin,
glycerin, magnesium silicate, sodium caseinate, soy lecithin, sodium
chloride, tricalcium phosphate, dipotassium phosphate, sodium stearoyl
lactylate, carrageenan, monoglyceride, diglyceride, pregelatinized
starch, hydroxypropylmethylcellulose, hydroxypropylmethylcellulose
acetate stearate, sugars such as sucrose, microcrystalline cellulose,
lactose, mannitol, polyvinylpyrrolidone (PVP), cholesterol, cholesterol
esters, sodium caseinate, soy lecithin, taurocholic acid,
phosp
hotidylcholine, cellulose and cellulose conjugates, sodium stearoyl
lactylate, carrageenan, monoglyceride, diglyceride, pregelatinized
starch, and the like. See, e.g., Remington: The Science and Practice of
Pharmacy, Nineteenth Ed (Easton, Pa.: Mack Publishing Company, 1995);
Hoover, John E., Remington's Pharmaceutical Sciences, Mack Publishing
Co., Easton, Pa. 1975; Liberman, H. A. and Lachman, L., Eds.,
Pharmaceutical Dosage Forms, Marcel Decker, New York, N.Y., 1980; and
Pharmaceutical Dosage Forms and Drug Delivery Systems, Seventh Ed.
(Lippincott Williams & Wilkins 1999).
[0195]Suitable filling agents for use in the solid dosage forms described
herein include, but are not limited to, lactose, calcium carbonate,
calcium phosphate, dibasic calcium phosphate, calcium sulfate,
microcrystalline cellulose (e.g., Avicel.RTM., Avicel.RTM. PH101,
Avicel.RTM.PH102, Avicel.RTM. PH1105, etc.), cellulose powder, dextrose,
dextrates, dextran, starches, pregelatinized starch,
hydroxypropylmethylcellulose (HPMC), hydroxypropylmethylcellulose
phthalate, hydroxypropylmethylcellulose acetate stearate (HPMCAS),
sucrose, xylitol, lactitol, mannitol, sorbitol, sodium chloride,
polyethylene glycol, and the like.
[0196]"Diluents" increase bulk of the composition to facilitate
compression or create sufficient bulk for homogenous blend for capsule
filling. Such compounds include e.g., lactose, starch, mannitol,
sorbitol, dextrose, microcrystalline cellulose such as Avicel.RTM.;
dibasic calcium phosphate, dicalcium phosphate dihydrate; tricalcium
phosphate, calcium phosphate; anhydrous lactose, spray-dried lactose;
pregelatinized starch, compressible sugar, such as Di-Pac.RTM. (Amstar);
mannitol, hydroxypropylmethylcellulose, hydroxypropylmethylcellulose
acetate stearate, sucrose-based diluents, confectioner's sugar; monobasic
calcium sulfate monohydrate, calcium sulfate dihydrate; calcium lactate
trihydrate, dextrates; hydrolyzed cereal solids, amylose; powdered
cellulose, calcium carbonate; glycine, kaolin; mannitol, sodium chloride;
inositol, bentonite, polysaccharides (including dextrates and
maltodextrin), polyols (including mannitol, xylitol, and sorbitol),
cyclodextrins, and the like. Non water-soluble diluents are compounds
typically used in the formulation of pharmaceuticals, such as calcium
phosphate, calcium sulfate, starches, modified starches and
microcrystalline cellulose, and microcellulose (e.g., having a density of
about 0.45 g/cm.sup.3, e.g. Avicel, powdered cellulose), and talc.
Combinations of one or more diluents can also be used.
[0197]"Plasticizers" are compounds used to soften the microencapsulation
material, film coatings or pharmaceutical blends for compression to make
them less brittle. Suitable plasticizers include, e.g., polyethylene
glycols such as PEG 300, PEG 400, PEG 600, PEG 1450, PEG 3350, and PEG
800, stearic acid, propylene glycol, oleic acid, triethyl cellulose and
triacetin. In some embodiments, plasticizers can also function as
dispersing agents or wetting agents.
[0198]"Surfactants or Wetting agents" also referred to as surface
stabilizers include compounds such as sodium lauryl sulfate, sodium
doccusate, triacetin, vitamin E TPGS, dioctylsulfosuccinate, gelatin,
casein, lecithin (phosphatides), dextran, gum acacia, cholesterol,
tragacanth, stearic acid, benzalkonium chloride, calcium stearate,
glycerol monostearate, cetostearyl alcohol, cetomacrogol emulsifying wax,
sorbitan esters, polyoxyethylene alkyl ethers (e.g., macrogol ethers such
as cetomacrogol 1000), polyoxyethylene castor oil derivatives,
polyoxyethylene sorbitan fatty acid esters (e.g., the commercially
available Tweens.RTM. such as e.g., Tween.RTM. 20, 60 and 80 (ICI
Speciality Chemicals)); polyethylene glycols (e.g., Carbowaxs 3550.RTM.
and 934.RTM. (Union Carbide)), polyoxyethylene stearates, colloidal
silicon dioxide, phosphates, carboxymethylcellulose calcium,
carboxymethylcellulose sodium, methylcellulose, hydroxyethylcellulose,
hydroxypropyl methylcellulose, hydroxypropylcellulose,
polyvinylpyrrolidone, hydroxypropylmethylcellulose phthalate,
noncrystalline cellulose, magnesium aluminium silicate, triethanolamine,
polyvinyl alcohol (PVA), 4-(1,1,3,3-tetramethylbutyl)-phenol polymer with
ethylene oxide and formaldehyde (also known as tyloxapol, superione, and
triton), poloxamers (e.g., Pluronics F68.RTM. and F108.RTM., which are
block copolymers of ethylene oxide and propylene oxide); poloxamines
(e.g., Tetronic 908.RTM., also known as Poloxamine 9085.RTM., which is a
tetrafunctional block copolymer derived from sequential addition of
propylene oxide and ethylene oxide to ethylenediamine (BASF Wyandotte
Corporation, Parsippany, N.J.)); Tetronic 1508.RTM. (T-1508, a
poloxamine) (BASF Wyandotte Corporation), Tritons X-200.RTM., which is an
alkyl aryl polyether sulfonate (Rohm and Haas); Crodestas F-110.RTM.,
which is a mixture of sucrose stearate and sucrose distearate (Croda
Inc.); p-isononylphenoxypoly-(glycidol), also known as Olin-IOG.RTM. or
Surfactant 10-G.RTM. (Olin Chemicals, Stamford, Conn.); Crodestas
SL-40.RTM. (Croda, Inc.); and SA90HCO, which is
C.sub.18H.sub.37CH.sub.2C(O)N(CH.sub.3)--CH.sub.2(CH.sub.2OH).sub.4(CH.su-
b.2OH).sub.2 (Eastman Kodak Co.); decanoyl-N-methylglucamide; n-decyl
.beta.-D-glucopyranoside; n-decyl .beta.-D-maltopyranoside; n-dodecyl
.beta.-D-glucopyranoside; n-dodecyl .beta.-D-maltoside;
heptanoyl-N-methylglucamide; n-heptyl-.beta.-D-glucopyranoside; n-heptyl
.beta.-D-thioglucoside; n-hexyl .beta.-D-glucopyranoside;
nonanoyl-N-methylglucamide; n-noyl .beta.-D-glucopyranoside;
octanoyl-N-methylglucamide; n-octyl-.beta.-D-glucopyranoside; octyl
.beta.-D-thioglucopyranoside; PEG-phospholipid, PEG-cholesterol,
PEG-cholesterol derivative, PEG-vitamin A, PEG-vitamin E, lysozyme,
random copolymers of vinyl pyrrolidone and vinyl acetate. The above
surfactants are commercially available or can be prepared by techniques
known in the art. Many are described in detail in the Handbook of
Pharmaceutical Excipients, published jointly by the American
Pharmaceutical Association and The Pharmaceutical Society of Great
Britain (The Pharmaceutical Press, 2000), specifically incorporated by
reference. Wetting agents include surfactants.
[0199]"Antifoaming agents" reduce foaming during processing which can
result in coagulation of aqueous dispersions, bubbles in the finished
form, or generally impair processing. Exemplary anti-foaming agents
include silicon emulsions or sorbitan sesquoleate.
[0200]"Antioxidants" include, e.g., butylated hydroxytoluene (BHT),
butylhydroxyanisole (BHA), ascorbic acid, sodium ascorbate, and
tocopherol. Combinations of one or more antioxidants can also be used.
[0201]Because the drugs utilized in certain embodiments of the present
invention have low solubility, they exhibit a strong correlation between
the rate of dissolution and bioavailability. Thus, it is important to
optimize the rate of dissolution in biological matrices in order to
enhance in vivo drug absorption. In order to release the drug from a
solid dosage form matrix as efficiently as possible, disintegrants are
often used in the formulation, especially when the dosage forms are
compressed with binder. Disintegrants help rupturing the dosage form
matrix by swelling or capillary action when moisture is absorbed into the
dosage form. In some embodiments of the invention, the solid dosage drug
formulation has greater than about 1 w % of a disintegrant. In various
embodiments of the present invention, the solid dose drug formulations
have between about 1 w % to about 11 w % or between about 2 wt % to about
8 wt % disintegrant. In yet other embodiments, the drug formulations have
greater than about 2 wt % disintegrant. In some embodiments, combinations
of disintegrants provide superior dispersion characteristics compared to
single disintegrant at a similar total weight percentage.
[0202]Suitable disintegrants for use in the solid dosage forms described
herein include, but are not limited to, natural starch such as corn
starch or potato starch, a pregelatinized starch such as National 1551 or
Amijel.RTM., or a sodium starch glycolate such as Promogel.RTM. or
Explotab.RTM., a cellulose such as a wood product, microcrystalline
cellulose, e.g., Avicel.RTM., Avicel.RTM. PH101, Avicel.RTM. PH102,
Avicel.RTM. PH105, Elcema.RTM. P100, Emcocel.RTM., Vivacel.RTM., Ming
Tia.RTM., and Solka-Floc.RTM., methylcellulose, croscarmellose, or a
cross-linked cellulose, such as cross-linked sodium
carboxymethylcellulose (Ac-Di-Sol.RTM.), cross-linked
carboxymethylcellulose, or cross-linked croscarmellose, a cross-linked
starch such as sodium starch glycolate, a cross-linked polymer such as
crosspovidone, a cross-linked polyvinylpyrrolidone, alginate such as
alginic acid or a salt of alginic acid such as sodium alginate, a clay
such as Veegum.RTM. HV (magnesium aluminum silicate), a gum such as agar,
guar, locust bean, Karaya, pectin, or tragacanth, sodium starch
glycolate, bentonite, a natural sponge, a surfactant, a resin such as a
cation-exchange resin, citrus pulp, sodium lauryl sulfate, sodium lauryl
sulfate in combination starch, and the like.
[0203]In one embodiment, Ac-Di-Sol is the disintegrant. The amount of
Ac-Di-Sol used in direct compression tableting may vary with typical
usage levels between 1 and 3 percent. When added to granulations,
generally the same percent is used as with a direct compression
formulation. It is often added to both the wet and dried granulations and
blends. The amount of Ac-Di-Sol used in capsule formulations generally
ranges from 3-6 percent. Reduced interparticle contact within a capsule
facilitates the need for elevated levels of disintegrant. Capsules filled
on automatic dosater types of equipment, as opposed to semi-automatic or
hand-filled machines, are more dense and have a harder structure due to
the greater compressional forces needed to form the plug and successfully
transfer it into the gelatin or HPMC shell. Greater plug hardness results
in greater effectiveness of Ac-Di-Sol.
[0204]Binders impart cohesiveness to solid oral dosage form formulations:
for powder filled capsule formulation, they aid in plug formation that
can be filled into soft or hard shell capsules and in tablet formulation,
binders ensure that the tablet remains intact after compression and help
assure blend uniformity prior to a compression or fill step. Materials
suitable for use as binders in the solid dosage forms described herein
include, but are not limited to, carboxymethylcellulose, methylcellulose
(e.g., Methocel.RTM.), hydroxypropylmethylcellulose (e.g. Hypromellose
USP Pharmacoat-603), hydroxypropylmethylcellulose acetate stearate
(Aqoate HS-LF and HS), hydroxyethylcellulose, hydroxypropylcellulose
(e.g., Klucel.RTM.), ethylcellulose (e.g., Ethocel.RTM.), and
microcrystalline cellulose (e.g., Avicel.RTM.), microcrystalline
dextrose, amylose, magnesium aluminum silicate, polysaccharide acids,
bentonites, gelatin, polyvinylpyrrolidone/vinyl acetate copolymer,
crosspovidone, povidone, starch, pregelatinized starch, tragacanth,
dextrin, a sugar, such as sucrose (e.g., Dipac.RTM.), glucose, dextrose,
molasses, mannitol, sorbitol, xylitol (e.g., Xylitab.RTM.), lactose, a
natural or synthetic gum such as acacia, tragacanth, ghatti gum, mucilage
of isapol husks, starch, polyvinylpyrrolidone (e.g., Povidone.RTM. CL,
Kollidon.RTM. CL, Polyplasdone.RTM. XL-10, and Povidone.RTM. K-12), larch
arabogalactan, Veegum.RTM., polyethylene glycol, waxes, sodium alginate,
and the like.
[0205]In general, binder levels of 20-70% are used in powder-filled
gelatin capsule formulations. Binder usage level in tablet formulations
is a function of whether direct compression, wet granulation, roller
compaction, or usage of other excipients such as fillers which itself can
act as moderate binder are used. Formulators skilled in art can determine
the binder level for the formulations, but binder usage level of up to
70% in tablet formulations is common.
[0206]Suitable lubricants or glidants for use in the solid dosage forms
described herein include, but are not limited to, stearic acid, calcium
hydroxide, talc, corn starch, sodium stearyl fumarate, alkali-metal and
alkaline earth metal salts, such as aluminum, calcium, magnesium, zinc,
stearic acid, sodium stearates, magnesium stearate, zinc stearate, waxes,
Stearowet.RTM., boric acid, sodium benzoate, sodium acetate, sodium
chloride, leucine, a polyethylene glycol or a methoxypolyethylene glycol
such as Carbowax.TM., PEG 4000, PEG 5000, PEG 6000, propylene glycol,
sodium oleate, glyceryl behenate, glyceryl palmitostearate, glyceryl
benzoate, magnesium or sodium lauryl sulfate, mineral oil, hydrogenated
vegetable oil such as hydrogenated soybean oil (Sterotex.RTM.), higher
fatty acids and their alkali-metal and alkaline earth metal salts, such
as aluminum, calcium, magnesium, zinc, stearic acid, sodium stearates,
glycerol, talc, Stearowet.RTM., colloidal silica such as Syloid.TM.,
Cab-O-Sil.RTM., a starch such as corn starch, silicone oil, a surfactant,
and the like.
[0207]Suitable suspending agents for use in the solid dosage forms
described here include, but are not limited to, polyvinylpyrrolidone,
e.g., polyvinylpyrrolidone K12, polyvinylpyrrolidone K17,
polyvinylpyrrolidone K25, or polyvinylpyrrolidone K30, polyethylene
glycol, e.g., the polyethylene glycol can have a molecular weight of
about 300 to about 6000, or about 3350 to about 4000, or about 7000 to
about 18000, vinyl pyrrolidone/vinyl acetate copolymer (S630), sodium
alginate, gums, such as, e.g., gum tragacanth and gum acacia, guar gum,
xanthans, including xanthan gum, sugars, cellulosics, such as, e.g.,
sodium carboxymethylcellulose, methylcellulose,
hydroxypropylmethylcellulose, hydroxyethylcellulose, polysorbate-80,
polyethoxylated sorbitan monolaurate, polyethoxylated sorbitan
monolaurate, povidone and the like.
[0208]Suitable antioxidants for use in the solid dosage forms described
herein include, for example, e.g., butylated hydroxytoluene (BHT),
butylhydroxyanisole (BHA), sodium ascorbate, Vitamin E TPGS, ascorbic
acid, sorbic acid and tocopherol.
[0209]"Erosion facilitators" include materials that control the erosion of
a particular material in gastrointestinal fluid. Erosion facilitators are
generally known to those of ordinary skill in the art. Exemplary erosion
facilitators include, e.g., hydrophilic polymers, electrolytes, proteins,
peptides, and amino acids. Combinations of one or more erosion
facilitator with one or more diffusion facilitator can also be used in
the present invention.
[0210]It should be appreciated that there is considerable overlap between
additives used in the solid dosage forms described herein. Thus, the
above-listed additives should be taken as merely exemplary, and not
limiting, of the types of additives that can be included in solid dosage
forms of the present invention. The amounts of such additives can be
readily determined by one skilled in the art, according to the particular
properties desired.
[0211]In embodiments directed to solid dosage forms utilizing substrates,
the substrates can be, e.g., inert beads, or can be selected from the
group consisting of lactose, calcium carbonate, calcium phosphate,
dibasic calcium phosphate, calcium sulfate, microcrystalline cellulose,
cellulose powder, dextrose, dextrates, dextran, starches, pregelatinized
starch, sucrose, xylitol, lactitol, mannitol, sorbitol, sodium chloride,
polyethylene glycol and mixtures thereof.
[0212]In embodiments directed to sustained or delayed dosage forms, the
dosage form can be a granulation comprising the drug particles and the
controlled release material, (e.g., hydrophobic polymer or pH dependent
material), the granulation compressed into a tablet or filled into a
capsule.
[0213]In other embodiments directed to sustained or delayed release dosage
forms, the dosage form can be a plurality of pharmaceutically acceptable
beads coated with the drug particles and overcoated with the controlled
release material, (e.g., hydrophobic polymer or pH dependent material),
the overcoated beads compressed into a tablet or filled into a capsule.
[0214]In other embodiments, one or more layers of the pharmaceutical
formulation are plasticized. Illustratively, a plasticizer is generally a
high boiling point solid or liquid. Suitable plasticizers can be added
from about 0.01% to about 50% by weight (w/w) of the coating composition.
Plasticizers include, but are not limited to, diethyl phthalate, citrate
esters, polyethylene glycol, glycerol, acetylated glycerides, triacetin,
polypropylene glycol, polyethylene glycol, triethyl citrate, dibutyl
sebacate, stearic acid, stearol, stearate, and castor oil.
Compressed Tablets
[0215]Compressed tablets are solid dosage forms prepared by compacting the
bulk blend drug formulations described above. In various embodiments,
compressed tablets which are designed to dissolve in the mouth will
comprise one or more flavoring agents. In other embodiments, the
compressed tablets will comprise a film surrounding the final compressed
tablet. In some embodiments, the film coating can provide a delayed
release of the drug formulation. In other embodiments, the film coating
aids in patient compliance (e.g., Opadry.RTM. coatings or sugar coating).
Film coatings comprising Opadry.RTM. typically range from about 1% to
about 3% of the tablet weight. Film coatings for delayed release usually
comprise 2-6% of a tablet weight or 7-15% of a spray-layered bead weight.
In other embodiments, the compressed tablets comprise one or more
excipients.
Capsule Formulations
[0216]A capsule may be prepared, e.g., by placing the bulk blend drug
formulation, described above, inside of a capsule. In some embodiments,
the drug formulations (non-aqueous suspensions and solutions) are placed
in a soft gelatin capsule. In other embodiments, the drug formulations
are placed in standard gelatin capsules or non-gelatin capsules such as
capsules comprising HPMC. In other embodiments, the drug formulations are
placed in a sprinkle capsule, wherein the capsule may be swallowed whole
or the capsule may be opened and the contents sprinkled on food prior to
eating. In some embodiments of the present invention, the therapeutic
dose is split into multiple (e.g., two, three, or four) capsules. In some
embodiments, the entire dose of the drug formulation is delivered in a
capsule form. For example, the capsule may comprise e.g., from 0.01 mg to
about 5 grams or any dose known to one skilled in the art, such as
between about 100 mg to about 600 mg of drug. In some embodiments, the
capsule may comprise between about 100 to about 500 mg of drug. In other
embodiments, capsule may comprise about 300 mg to about 400 mg of drug.
[0217]Another useful capsule has a shell comprising the material of the
rate-limiting membrane, including any of the coating materials previously
discussed, and filled with drug particles. A particular advantage of this
configuration is that the capsule may be prepared independently of the
drug particles, thus process conditions that would adversely affect the
drug can be used to prepare the capsule. A preferred embodiment is a
capsule having a shell made of a porous or a pH-sensitive polymer made by
a thermal forming process. An especially preferred embodiment is a
capsule shell in the form of an asymmetric membrane; i.e., a membrane
that has a thin skin on one surface and most of whose thickness is
constituted of a highly permeable porous material. A preferred process
for preparation of asymmetric membrane capsules comprises a solvent
exchange phase inversion, wherein a solution of polymer, coated on a
capsule-shaped mold, is induced to phase-separate by exchanging the
solvent with a miscible non-solvent. Examples of asymmetric membranes are
disclosed in the European Patent Specification 0 357 369 B1.
[0218]Yet another useful capsule, a "swelling plug device", can be used.
Drug particles can be incorporated into a non-dissolving capsule-half of
the device, which is sealed at one end by a hydrogel plug. This hydrogel
plug swells in an aqueous environment, and, after swelling for a
predetermined time, exits the capsule thus opening a port through which
the drug can leave the capsule and be delivered to the aqueous
environment. Preferred hydrogel-plugged capsules are those which exhibit
substantially no release of drug from the dosage form until the dosage
form has exited the stomach and has resided in the small intestine for
about 15 minutes or greater, preferably about 30 minutes or greater, thus
assuring that minimal drug is released in the stomach. Hydrogel-plugged
capsules of this type have been described in patent application
WO90/19168, which is incorporated herein by reference. A drug swelling
plug device may be prepared by loading drug into a non-dissolving
half-capsule shell which may be formed from a wide variety of materials,
including but not limited to polyethylene, polypropylene,
poly(methylmethacrylate), polyvinylchloride, polystyrene, polyurethanes,
polytetrafluoroethylene, nylons, polyformaldehydes, polyesters, cellulose
acetate, and nitrocellulose. The open end of the capsule shell is then
"plugged" with a cylindrical plug formed from a hydrogel-forming
material, including but not limited to, a homo- or co-poly(alkylene
oxide) cross linked by reaction with isocyanate or unsaturated cyclic
ether groups, as described in PCT Application WO 90/09168. The
composition and length of the hydrogel "plug" is selected to minimize
release of drug to the stomach, to decrease the incidence and/or severity
of gastrointestinal side effects. The plugged capsule-half is finally
sealed with a water-soluble, e.g., gelatin, capsule-half placed over the
hydrogel-plugged end of the drug-containing non-dissolving capsule-half.
In an embodiment of the "swelling plug device", the sealed device is
coated with a pH-sensitive enteric polymer or polymer mixture, for
example cellulose acetate phthalate or copolymers of methacrylic acid and
methylmethacrylate. The weight of the enteric polymer coat will generally
be from 2 to 20 wt %, preferably from 4 to 15 wt % of the weight of the
uncoated sealed capsule. When this preferred "enteric-coated swelling
plug device" is ingested orally, the enteric coat prevents release drug
in the stomach. The enteric coat dissolves quickly, e.g., within about 15
minutes, in the duodenum, triggering swelling of the hydrogel plug,
exiting of the hydrogel plug, and release of the incorporated drug into
the gastrointestinal tract at a time greater than about 15 minutes after,
and preferably greater than about 30 minutes after, the dosage form has
passed from the stomach into the duodenum. Prototype unfilled "swelling
plug devices" may be obtained from Scherer DDS Limited, Clydebank,
Scotland, under the designation Pulsincap.TM..
[0219]In another embodiment, a drug complex formulation comprising a dried
drug complex granulation can be filled in a capsule. Drug complex
particle suspension comprising 10 to 30 wt % drug, 1 to 10 wt %
hydroxypropylmethyl cellulose (Pharmacoat 603), 0.05 to 0.5 wt % sodium
lauryl sulfate, 0.015 to 0.2 wt % paraben such as methylparaben, 0.001 to
0.05 wt % simethicone emulsion (30% in water) 0.5 to 5% sucrose and 0.1
to 2% NaCl in water is pumped into a spray granulator using standard
parameters known by those skilled in the art. Each wt % of the drug
complex particle suspension is based on the total weight of the
suspension. The water is evaporated under vacuum at a temperature of
70.degree. C. to 90.degree. C. The resulting drug complex granulation
comprises about 50-80 wt % of drug based on the total weight of the
solid. Additional excipients such as magnesium stearate, Mannitol and a
disintegrant can be added for flow and re-dispersion properties. The
dispersed solid (in SGF or SIF) generally have a median particle size
(D50) of about 50 nm to about 1000 nm, more specifically, about 100 nm to
about 500 nm. In one embodiment, the capsule is a swelling plug device.
In another embodiment, the swelling plug device is further coated with
cellulose acetate phthalate or copolymers of methacrylic acid and
methylmethacrylate.
[0220]In yet another embodiment, spray layered drug particles or spray
layered drug complex particles are filled in a capsule. An exemplary
process for manufacturing the spray layered drug or drug complex
particles is the fluidized bed spraying process. Drug suspensions or drug
complex suspensions described above are sprayed onto sugar or
microcrystalline cellulose (MCC) beads (20-35 mesh) with Wurster column
insert at an inlet temperature of 50 to 60.degree. C. and air temp of 30
to 50.degree. C. A 15 to 20 wt % total solids content suspension
containing 45 to 80 wt % drug, 10 to 25 wt % hydroxypropylmethyl
cellulose, 0.25 to 2 wt % of SLS, 10 to 18 wt % of sucrose, 0.01 to 0.3
wt % simethicone emulsion (30% emulsion) and 0.3 to 10% NaCl, based on
the total weight of the solid content of the suspension, are sprayed
(bottom spray) onto the beads through 1.2 mm nozzles at 10 mL/min and 1.5
bar of pressure until a layering of 400 to 700% wt % is achieved as
compared to initial beads weight. The resulting spray layered drug
particles or drug complex particles comprise about 30 to 70 wt % of drug
based on the total weight of the particles. In one embodiment the capsule
is a size 0 soft gelatin capsule In one embodiment, the capsule is a
swelling plug device. In another embodiment, the swelling plug device is
further coated with cellulose acetate phthalate or copolymers of
methacrylic acid and methylmethacrylate.
[0221]In some embodiments the capsule includes at least 250 mg (or at
least 300 mg or at least 400 mg) drug and has a total weight of less than
800 mg (or less that 700 mg). The capsule may contain a plurality of
drug-containing beads, for example spray layered beads. In some
embodiments the beads are 12-25% drug by weight. In some embodiments some
or all of the drug containing beads are coated with a coating comprising
6 to 15% (or 8 to 12%) of the total bead weight. Optimization work
typically involves lower loading levels and the beads constitute 30 to
60% of the finished bead weight. Instead of or in addition to drug
containing beads the capsule may contain a granulated drug composition,
wherein the granulated composition comprises drug, or drug, and an ionic
dispersion modulator. In some embodiments the compositions additionally
comprise a complexing agent and an inorganic or organic salt. For example
the granulated composition in some embodiments is comprised of 0.3 to 20%
(or 1 to 10% or 1 to 5%) by weight inorganic or organic salt. These
granulations also typically contain 5% to 30% of a binding agent, 2% to
25% of a water soluble spacing agent and a wetting agent (0.5% to 2%) of
the total composition.
[0222]The capsule may be pulsatile release drug oral dosage form,
comprising: (a) a first dosage unit comprising a first drug dose that is
released substantially immediately following oral administration of the
dosage form to a patient; (b) a second dosage unit comprising a second
drug dose that is released approximately 3 to 7 hours following
administration of the dosage form to a patient. For pulsatile release
capsules containing beads that can be coated with a coating comprising 6
to 15% (or 8 to 12%) of the total bead weight. In some embodiments the
coating is a coating that is insoluble at pH 1 to 2 and soluble at pH
greater than 5.5.
[0223]In certain embodiments the pulsatile release capsule comprises by
weight 30 to 50% of the first drug dose and 50 to 70% of the second drug
dose. This pulsatile release capsule may contain a plurality of beads in
which some beads are immediate release beads and other beads are
formulated, for example with the use of a coating, for modified release,
typically 3 to 10 hours after administration. In other embodiments the
pulsatile release capsule contains a plurality of beads formulated for
modified release and drug powder, for example spray granulated drug, for
immediate release.
[0224]The particles disclosed above can be prepared according to any of
the methods disclosed herein or by the methods described in U.S. Pat.
Nos. 6,375,986; 6,428,814; 6,432,381; 6,592,903; 6,908,626; or 6,969,529;
the disclosures of which are hereby incorporated by reference.
[0225]In certain embodiments, the invention is directed to a
pharmaceutical composition comprising particles comprising (i) drug
thereof, (ii) a polymer selected from the group consisting of
polyvinylpyrrolidone, polysaccharides, copolymers of vinyl acetate and
vinyl pyrrolidone, polyvinyl alcohol, copolymers of vinyl acetate and
vinyl alcohol, carboxyalkylcelluloses, cellulosic polymers and mixtures
thereof, and (iii) a material selected from the group consisting of
sodium lauryl sulfate and dioctyl sodium sulfosuccinate (DOSS) and (iv)
an ionic dispersion modulator and (v) a water soluble spacer, wherein the
D50 of the particles by weight have an effective particle size of less
than about 500 nm (or any effective particle size, range, or any other
characteristic as disclosed herein), wherein the composition comprises
(a) an immediate release component comprising a first portion of the
particles and providing an immediate release of the drug or
pharmaceutically acceptable salt thereof; and (b) a controlled release
component comprising a second portion of the particles and providing a
controlled release of the drug or pharmaceutically acceptable salt
thereof.
Formulations Containing Coated Drug Particles
[0226]In some embodiments, the spray layered drug particles or spray
layered drug complex particles present in drug formulations, such as the
capsule formulation described above, is coated. Drug particles can be
with a modified release coating, such as an enteric coating using
cellulose acetate phthalate or copolymers of methacrylic acid and
methylmethacrylate. In one embodiment, the enteric coating may be present
in an amount of about 0.5 to 15 wt %, more specifically, about 8 to 12 wt
%, based on the weight of the spray layered particles. In one embodiment,
the spray layered drug particles or spray layered drug complex particles
coated with the enteric coatings can be filled in a modified release
capsule in which both enteric coated and immediate release drug beads are
filled into a soft gelatin capsule. Additional suitable excipients may
also be filled with the coated particles in the capsule.
[0227]In another embodiment, mixtures of spray layered drug particles or
spray layered drug complex particles coated with the enteric coatings and
those without the enteric coatings at appropriate ratios may be
encapsulated in a suitable immediate release capsule. The uncoated
particles release drug immediately upon administration while the coated
particles do not release drug until these particles reach intestine. By
controlling the ratios of the coated and uncoated particles, desirable
pulsatile release profiles may be obtained. In some embodiments, the
ratios between the uncoated and the coated particles are 20/80, or 30/70,
or 40/60, or 50/50, w/w to obtain desirable release.
Tablet Spray Layered or Spray Dried Dosage Forms
[0228]In some embodiments, the spray dried drug complex particles or spray
layered drug complex particles described above can be compressed into
tablets with commonly used pharmaceutical excipients. Any appropriate
apparatus for forming the coating can be used to make the enteric coated
tablets, e.g., fluidized bed coating using a wurster column, powder
layering in coating pans or rotary coaters; dry coating by double
compression technique; tablet coating by film coating technique, and the
like. See, e.g., U.S. Pat. No. 5,322,655; Remington's Pharmaceutical
Sciences Handbook: Chapter 90 "Coating of Pharmaceutical Dosage Forms",
1990.
[0229]In various embodiments, the spray dried drug complex particles or
spray layered drug complex particles described above and one or more
excipients are dry blended and compressed into a mass, such as a tablet,
having a hardness sufficient to provide a pharmaceutical composition that
substantially disintegrates within less than about 30 minutes, less than
about 35 minutes, less than about 40 minutes, less than about 45 minutes,
less than about 50 minutes, less than about 55 minutes, or less than
about 60 minutes, after oral administration, thereby releasing the drug
formulation into the gastrointestinal fluid.
[0230]In other embodiments, the spray dried drug complex particles or
spray layered drug complex particles with enteric coatings described
above and one or more excipients are dry blended and compressed into a
mass, such as a tablet. In one embodiment, the enteric coated particles
in the tablet substantially avoids release of drug, for example less than
15 wt %, in the stomach but releases substantially all drug (enterically
coated), for example, greater than 80 wt %, in the intestine.
[0231]In yet other embodiments, a pulsatile release drug formulation
comprises a first dosage unit comprising a formulation made from drug
containing granules made from a spray drying or spray granulated
procedure or a formulation made from drug complex containing granules
made from a spray drying or spray granulated procedure without enteric
coatings and a second dosage unit comprising spray dried drug complex
particles or spray layered drug complex particles with enteric coatings.
In one embodiment, the first dosage unit and the second dosage unit are
wet or dry blended and compressed into a mass to make a pulsatile release
tablet. In one embodiment, the weight ratio between the uncoated
particles and the coated particles is about -1:4 to 4:1.
[0232]In another embodiment, binding, lubricating and disintegrating
agents are blended (wet or dry) to the spray dried drug complex or drug
complex spray layered beads to make a compressible blend. The first and
the second dosage units are compressed separately and then compressed
together to form a bilayer tablet.
[0233]In yet another embodiment, the first dosage unit is in the form of
an overcoat and completely covers the second dosage unit.
Microencapsulated Formulations
[0234]In one aspect of the present invention, dosage forms may include
microencapsulated drug formulations. In some embodiments, one or more
other compatible materials are present in the microencapsulation
material. Exemplary materials include, but are not limited to, complexing
agents, ionic dispersion modulators, pH modifiers, erosion facilitators,
anti-foaming agents, antioxidants, flavoring agents, and carrier
materials such as binders, suspending agents, disintegration agents,
filling agents, surfactants, solubilizers, stabilizers, lubricants,
wetting agents, and diluents.
[0235]Materials useful for the microencapsulation described herein include
materials compatible with drug which sufficiently isolate drug from other
non-compatible excipients. Materials compatible with drug of the present
invention are those that delay the release of the drug in vivo.
[0236]Exemplary microencapsulation materials useful for delaying the
release of the formulations comprising drug include, but are not limited
to, hydroxypropyl cellulose ethers (HPC) such as Klucel.RTM. or Nisso
HPC, low-substituted hydroxypropyl cellulose ethers (L-HPC),
hydroxypropyl methyl cellulose ethers (HPMC) such as Seppifilm-LC,
Pharmacoat.RTM., Metolose SR, Methocel.RTM.-E, Opadry YS, PrimaFlo,
Benecel MP824, and Benecel MP843, methylcellulose polymers such as
Methocel.RTM.-A, hydroxypropylmethylcellulose acetate stearate Aqoat
(HF-LS, HF-LG, HF-MS) and Metolose.RTM., Ethylcelluloses (EC) and
mixtures thereof such as E461, Ethocel.RTM., Aqualon.RTM.-EC,
Surelease.RTM., Polyvinyl alcohol (PVA) such as Opadry AMB,
hydroxyethylcelluloses such as Natrosol.RTM., carboxymethylcelluloses and
salts of carboxymethylcelluloses (CMC) such as Aqualon.RTM.-CMC,
polyvinyl alcohol and polyethylene glycol co-polymers such as Kollicoat
IR.RTM., monoglycerides (Myverol), triglycerides (KLX), polyethylene
glycols, modified food starch, acrylic polymers and mixtures of acrylic
polymers with cellulose ethers such as Eudragit.RTM. EPO, Eudragit.RTM.
L30D-55, Eudragit.RTM. FS 30D Eudragit.RTM. L100-55, Eudragit.RTM. L100,
Eudragit.RTM. S100, Eudragit.RTM. RD100, Eudragit.RTM. E100,
Eudragit.RTM. L12.5, Eudragit.RTM. S12.5, Eudragit.RTM. NE30D, and
Eudragit.RTM. NE 40D, cellulose acetate phthalate, sepifilms such as
mixtures of HPMC and stearic acid, cyclodextrins, parabens, sodium
chloride, and mixtures of these materials.
[0237]In still other embodiments, plasticizers such as polyethylene
glycols, e.g., PEG 300, PEG 400, PEG 600, PEG 1450, PEG 3350, and PEG
800, stearic acid, propylene glycol, oleic acid, and triacetin are
incorporated into the microencapsulation material. In other embodiments,
the microencapsulating material useful for delaying the release of the
pharmaceutical compositions is from the USP or the National Formulary
(NF). In yet other embodiments, the microencapsulation material is
Klucel. In still other embodiments, the microencapsulation material is
methocel.
[0238]Microencapsulated drug may be formulated by methods known by one of
ordinary skill in the art. Such known methods include, e.g., spray drying
processes, spinning disk-solvent processes,
hot melt processes, spray
chilling methods, spray granulation via fluidized bed, electrostatic
deposition, centrifugal extrusion, rotational suspension separation,
polymerization at liquid-gas or solid-gas interface, pressure extrusion,
or spraying solvent extraction bath. In addition to these, several
chemical techniques, e.g., complex coacervation, solvent evaporation,
polymer-polymer incompatibility, interfacial polymerization in liquid
media, in situ polymerization, in-liquid drying, and desolvation in
liquid media could also be used. Furthermore, other methods such as
roller compaction, extrusion/spheronization, coacervation, or
nanoparticle coating may also be used.
[0239]The spinning disk method allows for: 1) an increased production rate
due to higher feed rates and use of higher solids loading in feed
solution, 2) the production of more spherical particles, 3) the
production of a more even coating, and 4) limited clogging of the spray
nozzle during the process.
[0240]Spray granulation via a fluid bed is often more readily available
for scale-up. In various embodiments, the material used in the
spray-granulation encapsulation process is emulsified or dispersed into
the core material in a concentrated form, e.g., 10-60% solids. The
microencapsulation material is, in one embodiment, emulsified until about
1 to 3 .mu.m droplets are obtained. Once a dispersion of drug and
encapsulation material is obtained, the emulsion is fed as droplets into
the heated chamber of the spray granulator. In some embodiments, the
droplets are sprayed into the chamber or spun off a rotating disk. The
microspheres are then dried in the heated chamber and fall to the bottom
of the chamber where they are harvested.
[0241]Roller compaction, which involves dry granulation of single powder
or a blended mixture of powders by the use of pressure to form dense
compacts (the compacts are subsequently milled to a desired particle
size), provides another alternative. It is a simple process that is
readily available for use, and does not involve the use of solvents for
granulation. Thus, roller compaction eliminates the exposure of sensitive
active pharmaceutical ingredients to moisture and drying. Roller
compaction can also provide some enhanced stability and taste-masking
characteristics to active pharmaceutical by diluting and isolating such
components in a granulated matrix of compatible ingredients. Roller
compaction also imparts increased density and flow to the powder.
[0242]Extrusion/spheronization is another method that involves wet massing
of active pharmaceutical ingredients, followed by the extrusion of the
wet mass through a perforated plate to produce short cylindrical rods.
These rods are subsequently placed into a rapidly rotating spheronizer to
shape the cylindrical rods into uniform spheres. The spheres are
subsequently dried using a fluid bed drier and then coated with a
functional coating using a fluid bed equipped with a Wurster insert and
spray nozzle.
[0243]Coacervation involves microencapsulation of materials such as active
pharmaceutical ingredients and involves a three part process of particle
or droplet formation, coacerate wall formation, and capsule isolation.
This method can produce very small particle size microcapsules (10-70
microns).
[0244]In one embodiment, the drug particles are microencapsulated prior to
being formulated into one of the above forms. In still another
embodiment, some or most of the drug particles are coated prior to being
further formulated by using standard coating procedures, such as those
described in Remington's Pharmaceutical Sciences, 20th Edition (2000).
Coated or Plasticized Formulations
[0245]In other embodiments, the solid dosage drug formulations are
plasticized (coated) with one or more layers. Illustratively, a
plasticizer is generally a high boiling point solid or liquid. Suitable
plasticizers can be added from about 0.01% to about 50% by weight (w/w)
of the coating composition. Plasticizers include, but are not limited to,
diethyl phthalate, citrate esters, polyethylene glycol, glycerol,
acetylated glycerides, triacetin, polypropylene glycol, polyethylene
glycol, triethyl citrate, dibutyl sebacate, stearic acid, stearol,
stearate, and castor oil.
[0246]In other embodiments a powder comprising the drug formulations
described herein may be formulated to comprise one or more pharmaceutical
excipients and flavors. Such a powder may be prepared, for example, by
mixing the drug formulation and optional pharmaceutical excipients to
form a bulk blend composition. Additional embodiments also comprise a
suspending agent and/or a wetting agent. This bulk blend is uniformly
subdivided into unit dosage packaging or multi-dosage packaging units.
The term "uniform" means the homogeneity of the bulk blend is
substantially maintained during the packaging process. In some
embodiments, at least about 75% to about 85% of the drug has an effective
particle size by weight of less than 500 nm to about 100 nm. In other
embodiments, the drug comprises at least 90% drug particles having an
effective particle size by weight of less than 500 nm to about 100 nm.
Effervescent Powders
[0247]In still other embodiments, effervescent powders are also prepared
in accordance with the present invention. Effervescent salts have been
used to disperse medicines in water for oral administration. Effervescent
salts are granules or coarse powders containing a medicinal agent in a
dry mixture, usually composed of sodium bicarbonate, citric acid and/or
tartaric acid. When salts of the present invention are added to water,
the acids and the base react to liberate carbon dioxide gas, thereby
causing "effervescence." Examples of effervescent salts include, e.g:
sodium bicarbonate or a mixture of sodium bicarbonate and sodium
carbonate, citric acid and/or tartaric acid. Any acid-base combination
that results in the liberation of carbon dioxide can be used in place of
the combination of sodium bicarbonate and citric and tartaric acids, as
long as the ingredients were suitable for pharmaceutical use and result
in a pH of about 6.0 or higher.
[0248]The method of preparation of the effervescent granules of the
present invention employs three basic processes: wet granulation, dry
granulation and fusion. The fusion method is used for the preparation of
most commercial effervescent powders. It should be noted that, although
these methods are intended for the preparation of granules, the
formulations of effervescent salts of the present invention could also be
prepared as tablets, according to known technology for tablet
preparation.
Wet and Dry Granulation
[0249]Wet granulation is one of the oldest methods of granule preparation.
The individual steps in the wet granulation process of tablet preparation
include milling and sieving of the ingredients, dry powder mixing, wet
massing, granulation, drying and final grinding. In various embodiments,
the drug composition is added to the other excipients of the
pharmaceutical formulation after they have been wet granulated.
[0250]Dry granulation involves compressing a powder mixture into a rough
tablet or "slug" on a heavy-duty rotary tablet press. The slugs are then
broken up into granular particles by a grinding operation, usually by
passage through an oscillation granulator. The individual steps include
mixing of the powders, compressing (slugging) and grinding (slug
reduction or granulation). No wet binder or moisture is involved in any
of the steps. In some embodiments, the drug formulation is dry granulated
with other excipients in the pharmaceutical formulation. In other
embodiments, the drug formulation is added to other excipients of the
pharmaceutical formulation after they have been dry granulated.
Solid Dispersions
[0251]In other embodiments, the drug formulations described herein are
solid dispersions. Methods of producing such solid dispersions are known
in the art and include, but are not limited to, for example, U.S. Pat.
Nos. 4,343,789, 5,340,591, 5,456,923, 5,700,485, 5,723,269, and U.S. Pub.
Appl 2004/0013734, each of which is specifically incorporated by
reference. In some embodiments, the solid dispersions of the invention
comprise both amorphous and non-amorphous drug and can have enhanced
bioavailability as compared to conventional drug formulations. In still
other embodiments, the drug formulations described herein are solid
solutions. Solid solutions incorporate a substance together with the
active agent and other excipients such that heating the mixture results
in dissolution of the drug and the resulting composition is then cooled
to provide a solid blend which can be further formulated or directly
added to a capsule or compressed into a tablet. Methods of producing such
solid solutions are known in the art and include, but are not limited to,
for example, U.S. Pat. Nos. 4,151,273, 5,281,420, and 6,083,518, each of
which is specifically incorporated by reference.
Modified Release Forms, Including Controlled Release and Delayed Release
[0252]The pharmaceutical solid oral dosage forms comprising the drug
formulations described herein can be immediate release, or can be further
formulated to provide a modified or controlled release of drug.
[0253]In certain embodiments, the controlled release component provides a
release selected from the group consisting of sustained release or
delayed release.
[0254]In certain embodiments, the controlled release component comprises a
coating comprising a hydrophobic material, coated on the second portion
of particles.
[0255]In certain embodiments, the controlled release component comprises a
matrix comprising the second portion of particles dispersed in a
hydrophobic material.
[0256]In certain embodiments, the immediate release component and the
controlled release component are independently selected from the group
consisting of a tablet, a pill, multiparticulates, a powder, a capsule, a
solid dispersion, a solid solution, a pellet, or a granule.
[0257]In certain embodiments, the hydrophobic material is selected from
the group consisting of an acrylic polymer, a cellulosic polymer,
shellac, zein, fatty alcohols, hydrogenated fats, fatty acid esters,
fatty acid glycerides, hydrocarbons, waxes, stearic acid, stearyl
alcohol, and mixtures thereof.
[0258]In certain embodiments, the hydrophobic material is an enteric
polymer.
[0259]In certain embodiments, the enteric polymer is selected from the
group consisting of shellac, acrylic polymers, cellulose derivatives,
polyvinyl acetate phthalate and mixtures thereof.
[0260]In certain embodiments, the delayed release component provides a
dose of the drug or pharmaceutically acceptable salt thereof delayed by
from about 2 hours to about 12 hours after administration.
[0261]In certain embodiments, the delayed release component provides a
dose of the drug or pharmaceutically acceptable salt thereof delayed by
from about 2 hours to about 8 hours after administration.
[0262]In certain embodiments, the delayed component provides a dose of the
drug or pharmaceutically acceptable salt thereof delayed by from about 3
hours to about 7 hours after administration.
[0263]In certain embodiments, the controlled release component provides a
sustained release of the drug or pharmaceutically acceptable salt thereof
for about 2 hours to about 6 hours after administration.
[0264]In certain embodiments, the controlled release component provides a
sustained release of the drug or pharmaceutically acceptable salt thereof
for about 3 hours to about 10 hours after administration.
[0265]In certain embodiments, the coating further comprises a plasticizer,
a colorant, a detackifier, a surfactant, an anti-foaming agent, a
lubricant or a mixture thereof.
[0266]In certain embodiments, the immediate release component and the
controlled release component independently comprise one or more
pharmaceutically acceptable additives from the group consisting of
carriers, binders, filling agents, suspending agents, flavoring agents,
sweetening agents, disintegrating agents, dispersing agents, surfactants,
lubricants, colorants, diluents, solubilizers, moistening agents,
plasticizers, stabilizers, penetration enhancers, wetting agents,
anti-foaming agents, antioxidants, preservatives, or one or more
combinations thereof.
[0267]The pharmaceutical dosage forms disclosed herein having an immediate
release component and a controlled release component in this section
(XIII) can provide any pharmacokinetic profile as disclosed herein.
[0268]In some embodiments, the solid dosage forms described herein can be
formulated as a delay release dosage form such as enteric coated delayed
release oral dosage forms, i.e., as an oral dosage form of a
pharmaceutical composition as described herein which utilizes an enteric
coating to affect release in the small intestine of the gastrointestinal
tract. The enteric coated dosage form may be a compressed or molded or
extruded tablet/mold (coated or uncoated) containing granules, powder,
pellets, beads or particles of the active ingredient and/or other
composition components, which are themselves coated or uncoated. The
enteric coated oral dosage form may also be a capsule (coated or
uncoated) containing pellets, beads or granules of the solid carrier or
the composition, which are themselves coated or uncoated. Enteric
coatings may also be used to prepare other controlled release dosage
forms including extended release and pulsatile release dosage forms.
[0269]An "enterically coated" formulation of drug is intended to mean that
some or most of the drug has been enterically coated to ensure that at
least some of the drug is released after entering the small intestine,
rather than the acidic environment of the stomach. In some embodiments,
about 40% to about 60% of the coated drug particles are released in the
middle region of the small intestine to minimize interaction with bile
acids and minimize food effects. In some embodiments, the enterically
coated formulations provide the release of greater than 80% of drug in
the small intestine.
[0270]The enteric coating material should be non-toxic and is
predominantly soluble in the intestinal fluid, but substantially
insoluble in the gastric fluids. Examples include polyvinyl acetate
phthalate (PVAP), commercially available under trade names of Opadry.RTM.
Enteric or Acryl-eze MP from Colorcon.RTM., hydroxypropylmethylcellulose
acetate succinate (HPMCAS), cellulose acetate phthalate (CAP),
methacrylic acid copolymer, hydroxypropylmethylcellulose succinate,
cellulose acetate succinate, cellulose acetate hexahydrophthalate,
hydroxypropylmethylcellulose hexahydrophthalate,
hydroxypropylmethylcellulose phthalate (HPMCP), cellulose propionate
phthalate, cellulose acetate maleate, cellulose acetate trimellitate,
cellulose acetate butyrate, cellulose acetate propionate, methacrylic
acid/methacrylate polymer, methacrylic acid-methyl methacrylate
copolymer, ethyl methacrylate-methylmethacrylate-chlorotrimethylammonium
ethyl methacrylate copolymer, and the like, and combinations comprising
one or more of the foregoing enteric polymers. Other examples include
natural resins, such as shellac, SANDARAC, copal collophorium, and
combinations comprising one or more of the foregoing polymers. Yet other
examples of enteric polymers include synthetic resin bearing carboxyl
groups. The methacrylic acid: acrylic acid ethyl ester copolymers are
commercially available under the trade names of "Eudragit.RTM. L", such
as Eudragit.RTM. L 30-D55 from Degussa.
[0271]Enteric coatings should be applied to a sufficient thickness such
that the entire coating does not appreciably dissolve in the
gastrointestinal fluids at pH below about 5 after 1 hour, but does
dissolve at pH about 5 and above. It is expected that any anionic polymer
exhibiting a pH-dependent solubility profile can be used as an enteric
coating in the practice of the present invention to achieve delivery to
the lower gastrointestinal tract. In some embodiments the polymers for
use in the present invention are anionic carboxylic polymers. In other
embodiments, the polymers and compatible mixtures thereof, and some of
their properties, include, but are not limited to: Shellac--also called
purified shellac, a refined product obtained from the resinous secretion
of an insect. This coating dissolves in media of pH>7; Acrylic
polymers: The performance of acrylic polymers (primarily their solubility
in biological fluids) can vary based on the degree and type of
substitution. Examples of suitable acrylic polymers include methacrylic
acid copolymers and ammonia methacrylate copolymers. The Eudragit series
E, L, S, RL, RS and NE (Rohm Pharma) are available as solubilized in
organic solvent, aqueous dispersion, or dry powders. The Eudragit series
RL, NE, and RS are insoluble in the gastrointestinal tract but are
permeable and are used primarily for colonic targeting. The Eudragit
series E dissolve in the stomach. The Eudragit series L, L-30D and S are
insoluble in stomach and dissolve in the intestine; Opadry Enteric are
also insoluble in stomach and dissolve in the intestine; Cellulose
Derivatives--Examples of suitable cellulose derivatives are: ethyl
cellulose; reaction mixtures of partial acetate esters of cellulose with
phthalic anhydride. The performance can vary based on the degree and type
of substitution. Cellulose acetate phthalate (CAP) dissolves in pH>6.
Aquateric (FMC) is an aqueous based system and is a spray dried CAP
psuedolatex with particles<1 .mu.m. Other components in Aquateric can
include pluronics, Tweens, and acetylated monoglycerides. Other suitable
cellulose derivatives include: cellulose acetate trimellitate (Eastman);
methylcellulose (Pharmacoat, Methocel); hydroxypropylmethyl cellulose
phthalate (HPMCP); hydroxypropylmethyl cellulose succinate (HPMCS); and
hydroxypropylmethylcellulose acetate succinate (e.g., AQOAT (Shin Etsu)).
The performance can vary based on the degree and type of substitution.
For example, HPMCP such as, HP-50, HP-55, HP-55S, HP-55F grades are
suitable. The performance can vary based on the degree and type of
substitution. For example, suitable grades of
hydroxypropylmethylcellulose acetate succinate include, but are not
limited to, AS-LG (LF), which dissolves at pH 5, AS-MG (MF), which
dissolves at pH 5.5, and AS-HG (HF), which dissolves at higher pH. These
polymers are offered as granules, or as fine powders for aqueous
dispersions; PolyVinyl Acetate Phthalate (PVAP). PVAP dissolves in
pH>5 and it is much less permeable to water vapor and gastric fluids.
[0272]In some embodiments, the coating can, and usually does, contain a
plasticizer and possibly other coating excipients such as colorants,
talc, and/or magnesium stearate, which are well known in the art.
Suitable plasticizers include triethyl citrate (Citroflex 2), triacetin
(glyceryl triacetate), acetyl triethyl citrate (Citroflec A2), Carbowax
400 (polyethylene glycol 400), diethyl phthalate, tributyl citrate,
acetylated monoglycerides, glycerol, fatty acid esters, propylene glycol,
and dibutyl phthalate. In particular, anionic carboxylic acrylic polymers
usually will contain 10-25% by weight of a plasticizer, especially
dibutyl phthalate, polyethylene glycol, triethyl citrate and triacetin.
Conventional coating techniques such as spray or pan coating are employed
to apply coatings. The coating thickness must be sufficient to ensure
that the oral dosage form remains intact until the desired site of
topical delivery in the intestinal tract is reached.
[0273]In other embodiments, the drug formulations described herein are
delivered using a pulsatile dosage form. In such a pulsatile release drug
oral dosage form, a first dose of the drug is released followed by a
second dose of the drug released approximately 3 to 7 hours following
administration of the dosage form. For example, such pulsatile dosage
forms may comprise: (a) a first dosage unit comprising a first dose of
drug that is released substantially immediately following oral
administration of the dosage form to a patient; (b) a second dosage unit
comprising a second dose of drug that is released approximately 3 to 7
hours following administration of the dosage form to a patient. Pulsatile
dosage forms comprising the drug formulations described herein may be
administered using a variety of formulations known in the art. For
example, such formulations include, but are not limited to, those
described in U.S. Pat. Nos. 5,011,692, 5,017,381, 5,229,135, and
5,840,329, each of which is specifically incorporated by reference. Other
dosage forms suitable for use with the drug formulations are described
in, for example, U.S. Pat. Nos. 4,871,549, 5,260,068, 5,260,069,
5,508,040, 5,567,441 and 5,837,284, all of which are specifically
incorporated by reference. In one embodiment, the controlled release
dosage form is pulsatile release solid oral dosage form comprising at
least two groups of particles, each containing the drug formulation
described herein. The first group of particles provides a substantially
immediate dose of drug upon ingestion by a subject. The first group of
particles can be either uncoated or comprise a coating and/or sealant.
The second group of particles comprises coated particles, which comprise
from about 2% to about 75%, preferably from about 2.5% to about 70%, and
more preferably from about 40% to about 70%, by weight of the total dose
of the drug in said formulation, in admixture with one or more binders.
The coating comprises a pharmaceutically acceptable ingredient in an
amount sufficient to provide a delay of from about 2 hours to about 7
hours following ingestion before release of the second dose. Suitable
coatings include one or more differentially degradable coatings such as,
by way of example only, pH sensitive coatings (enteric coatings) such as
acrylic resins (e.g., Eudragit.RTM. EPO, Eudragit.RTM. L30D-55,
Eudragit.RTM. FS 30D Eudragit.RTM. L100-55, Eudragit.RTM. L100,
Eudragit.RTM. S100, Eudragit.RTM. RD100, Eudragit.RTM. E100,
Eudragit.RTM. L12.5, Eudragit.RTM. S12.5, and Eudragit.RTM. NE30D,
Eudragit.RTM. NE 40D.RTM.) either alone or blended with cellulose
derivatives, e.g., ethylcellulose, or non-enteric coatings having
variable thickness to provide differential release of the drug
formulation.
[0274]Many other types of controlled release systems known to those of
ordinary skill in the art and are suitable for use with the drug
formulations described herein. Examples of such delivery systems include,
e.g., polymer-based systems, such as polylactic and polyglycolic acid,
polyanhydrides and polycaprolactone; porous matrices, nonpolymer-based
systems that are lipids, including sterols, such as cholesterol,
cholesterol esters and fatty acids, or neutral fats, such as mono-, di-
and triglycerides; hydrogel release systems; silastic systems;
peptide-based systems; wax coatings, bioerodible dosage forms, compressed
tablets using conventional binders and the like. See, e.g., Liberman et
al., Pharmaceutical Dosage Forms, 2.sup.nd Ed., Vol. 1, pp. 209-214
(1990); Singh et al., Encyclopedia of Pharmaceutical Technology, 2.sup.nd
Ed., pp. 751-753 (2002); U.S. Pat. Nos. 4,327,725, 4,624,848, 4,968,509,
5,461,140, 5,456,923, 5,516,527, 5,622,721, 5,686,105, 5,700,410,
5,977,175, 6,465,014 and 6,932,983, each of which is specifically
incorporated by reference.
[0275]In another embodiment, a modified release dosage formulation may
comprise a combination of: (a) a compressed tablet core comprising
complexed drug particles, a surface stabilizer, an ionic dispersion
modifier, a water soluble spacer, a pharmaceutically acceptable water
swellable polymer, and an osmotic agent; and (b) an outer coating layer
which completely covers the tablet core and comprises a pH sensitive
coating. An optional sealing coat may be applied to the compressed tablet
core and an optional coating layer comprising an enteric coating agent
may be applied under the outer coating layer as an inner coating or as an
overcoat over the outer coating layer. The tablet core may be compressed
using a smooth faced tablet die. In one embodiment, the active agent is
drug.
[0276]The osmotic agent in this dosage form is any non-toxic
pharmaceutically acceptable water soluble compound which will dissolve
sufficiently in water and increase the osmotic pressure inside the tablet
core. Suitable osmotic agents include simple sugars and salts such as
sodium chloride, potassium chloride, magnesium sulfate, magnesium
sulfate, magnesium chloride, sodium sulfate, lithium sulfate, urea,
inositol, sucrose, lactose, glucose, sorbitol, fructose, mannitol,
dextrose, magnesium succinate, potassium acid phosphate and the like. The
preferred osmotic agent for the tablet core is a simple sugar such as
anhydrous lactose in the range of 0-50% by weight, based on the weight of
the compressed, uncoated tablet.
[0277]The water swellable polymer may be any pharmaceutically acceptable
polymer which swells and expands in the presence of water to slowly
release drug. These polymers include polyethylene oxide, methylcellulose,
hydroxypropylcellulose, hydroxypropylmethylcellulose and the like. In a
preferred embodiment, the water swellable polymer will be polyethylene
oxide (obtained from Union Carbide Corporation under the trade name
Polyox WSR Coagulant or Polyox WSR N 80). These materials form a viscous
gel in water or other solvent system at a sufficient concentration to
control the release of the drug. This will generally require a
concentration of the pharmaceutically acceptable, water swellable polymer
of about 0-50% by weight of the compressed, uncoated tablet.
[0278]The outer coating comprises a pH sensitive coating which functions
as an enteric polymer in that it does not begin to dissolve until pH
conditions in excess of the pH of the stomach region are encountered. The
pH sensitive coating is the same type of material that is described
above. The pH sensitive coating may be present in an amount of about
0.5-15 wt %, more specifically, about 8-12 wt %, based on the weight of
the coated tablet core.
[0279]Certain controlled release formulation may release less than about
20 wt % of drug in the formulation within the first three hours after
administration and more than about 60 percent of drug between 3 and 10
hours. Other controlled release drug formulation may release less than
about 50 percent within the first three hours after administration and
about 50 percent of drug between 3 and 10 hours.
[0280]Colorants, detackifiers, surfactants, antifoaming agents, lubricants
(e.g., carnuba wax or PEG) may be added to the coatings besides
plasticizers to solubilize or disperse the coating material, and to
improve coating performance and the coated product.
[0281]A particularly suitable methacrylic copolymer is Eudragit L.RTM.,
particularly L-30D.RTM. and Eudragit 100-55.RTM., manufactured by Rohm
Pharma, Germany. In Eudragit L-30D.RTM., the ratio of free carboxyl
groups to ester groups is approximately 1:1. Further, the copolymer is
known to be insoluble in gastrointestinal fluids having pH below 5.5,
generally 1.5-5.5, i.e., the pH generally present in the fluid of the
upper gastrointestinal tract, but readily soluble or partially soluble at
pH above 5.5, i.e., the pH values present in the small intestine.
[0282]In some embodiments, materials include shellac, acrylic polymers,
cellulosic derivatives, polyvinyl acetate phthalate, and mixtures
thereof. In other embodiments, materials include Eudragit.RTM. series E,
L, RL, RS, NE, L, L300, S, 100-55, cellulose acetate phthalate,
Aquateric, cellulose acetate trimellitate, ethyl cellulose,
hydroxypropylmethylcellulose phthalate, hydroxypropylmethylcellulose
acetate succinate, polyvinyl acetate phthalate, and Cotteric.
[0283]In other aspects, the invention is directed to an oral solid dosage
form comprising (i) a controlled release component comprising a first
portion of particles comprising drug; and a controlled release material,
and (ii) an immediate release component comprising a second portion of
particles comprising drug, the first and second portion of drug particles
having a volume weighted median diameter (D50) of from about 50 nm to
about 1000 nm, from about 100 nm to about 450 nm, or from about 100 nm to
about 350 nm. The ratio of drug in controlled release to immediate
release can be, e.g., from about 4:1 to about 1:4, from about 3:2 to
about 2:3, or about 1:1. The controlled release component can be in any
form, including but not limited to (i) a plurality of pharmaceutically
acceptable beads coated with the first portion of drug particles and
overcoated with the controlled release material (optionally a film coat
comprising a material such as hydroxypropylmethylcellulose or polyvinyl
alcohol can be included on the beads prior to coating with the drug
particles), (ii) a plurality of matrices comprising the first portion of
drug particles dispersed in the controlled release material, (iii) a
tablet comprising the first portion of drug particles dispersed in the
controlled release material, or (iv) a granulation comprising the first
portion of drug particles and the controlled release material. The
immediate release component can be in any form, including but not limited
to (i) plurality of pharmaceutically acceptable beads coated with the
second portion of drug particles, (ii) a plurality of matrices comprising
the second portion of drug particles dispersed in an excipient, (iii) a
tablet comprising the second portion of drug particles dispersed in
excipient, or (v) a granulation comprising the second portion of drug
particles and excipient. Alternatively, the immediate release component
can be included in the dosage form in powder form.
[0284]In certain embodiments, the controlled release component and the
immediate release component are contained in a capsule.
[0285]In other embodiments, the controlled release component is a tablet
and the immediate release component is coated onto the tablet.
[0286]In further embodiments, the controlled release component and the
immediate release component are in a bi-layer tablet.
[0287]In still other embodiments, the controlled release component
comprises a plurality of pharmaceutically acceptable beads coated with
the first portion of drug particles and overcoated with the controlled
release material and the immediate release component comprises a
plurality of pharmaceutically acceptable beads coated with the second
portion of drug particles, the controlled release component and immediate
release component contained in a capsule.
[0288]In another aspect, the controlled release component comprises a
plurality of pharmaceutically acceptable beads coated with the first
portion of drug particles and overcoated with the controlled release
material and the immediate release component comprises a tablet
comprising the second portion of drug particles dispersed in an
excipient, the controlled release component and immediate release
component contained in a capsule.
[0289]In still another embodiments, controlled release component comprises
a plurality of pharmaceutically acceptable beads coated with the first
portion of drug particles and overcoated with the controlled release
material and the immediate release component comprises a granulation
comprising the second portion of drug particles and an excipient, the
controlled release component and immediate release component contained in
a capsule.
[0290]In another embodiment, the controlled release component comprises a
plurality of pharmaceutically acceptable beads coated with the first
portion of drug particles and overcoated with the controlled release
material, and the immediate release component comprises a granulation
comprising the second portion of drug particles and an excipient, the
controlled release component dispersed in the immediate release component
in the form of a compressed tablet.
[0291]In further embodiments, the controlled release component comprises a
compressed tablet and the immediate release component is compression
coated over the controlled release tablet.
[0292]In embodiments directed to drug coated beads, controlled release
material can be coated onto the drug layered bead in an amount, e.g.,
from about 3% to about 25%, or from about 10% to about 20%, based on the
total weight of the component.
[0293]In certain embodiments, the dosage forms of the present invention
provide pulsatile release of two or more doses of drug. The dosage form
can provide an immediate release dose after administration and at least
one additional dose at a time after administration selected from the
group consisting of 3-8 hours, 6-10 hours, 10-14 hours, 14-18 hours,
16-20 hours and 22-24 hours.
[0294]In certain embodiments, the invention is directed to an oral solid
dosage form comprising drug particles and a controlled release material,
the drug particles having a volume weighted median diameter (D50) of from
about 50 nm to about 1000 nm, the dosage form providing a controlled
release of the drug to provide a therapeutic effect for about 8 to about
24 hours after administration.
[0295]In other embodiments, the invention is directed to an oral solid
dosage form comprising particles comprising drug; and a pH dependent
polymer, the drug particles having a volume weighted median diameter
(D50) from about 50 nm to about 1000 nm, the dosage form providing a
delayed release of the drug for a time period from about 2 to about 12
hours after administration.
[0296]The dosage forms can be prepared according to any of the methods
disclosed herein or by the methods described in U.S. Pat. Nos. 5,209,746;
5,213,808; 5,221,278; 5,260,068; 5,260,069; 5,308,348; 5,312,390;
5,318,588; 5,340,590; 5,391,381; 5,456,679; 5,472,708; 5,508,040;
5,840,329; 5,980,508; 6,214,379; 6,228,398; 6,248,363; 6,514,518;
6,569,463; 6,607,751; 6,627,223; 6,730,325; 6,793,936; 6,902,742 and
6,923,988, the disclosures of which are hereby incorporated by reference.
Liquid Formulations
[0297]In some embodiments, pharmaceutical drug formulations are provided
comprising the drug particles described herein and at least one
dispersing agent or suspending agent for oral administration to a
subject. The drug formulation may be a powder and/or granules for
suspension, and upon admixture with water, a substantially uniform
suspension is obtained. As described herein, the aqueous dispersion can
comprise amorphous and non-amorphous drug particles of consisting of
multiple effective particle sizes such that drug particles having a
smaller effective particle size are absorbed more quickly and drug
particles having a larger effective particle size are absorbed more
slowly. In certain embodiments the aqueous dispersion or suspension is an
immediate release formulation. In another embodiment, an aqueous
dispersion comprising amorphous drug particles is formulated such that
about 50% of the drug particles are absorbed within about 3 hours after
administration and about 90% of the drug particles are absorbed within
about 10 hours after administration. In other embodiments, addition of a
complexing agent to the aqueous dispersion results in a larger span of
drug containing particles to extend the drug absorption phase such that
50-80% of the particles are absorbed in the first 3 hours and about 90%
are absorbed by about 10 hours.
[0298]A suspension is "substantially uniform" when it is mostly
homogenous, that is, when the suspension is composed of approximately the
same concentration of drug at any point throughout the suspension.
Preferred embodiments are those that provide concentrations essentially
the same (within 15%) when measured at various points in a drug aqueous
oral formulation after shaking. Especially preferred are aqueous
suspensions and dispersions, which maintain homogeneity (up to 15%
variation) when measured 2 hours after shaking. The homogeneity should be
determined by a sampling method consistent with regard to determining
homogeneity of the entire composition. In one embodiment, an aqueous
suspension can be re-suspended into a homogenous suspension by physical
agitation lasting less than 1 minute. In another embodiment, an aqueous
suspension can be re-suspended into a homogenous suspension by physical
agitation lasting less than 45 seconds. In yet another embodiment, an
aqueous suspension can be re-suspended into a homogenous suspension by
physical agitation lasting less than 30 seconds. In still another
embodiment, no agitation is necessary to maintain a homogeneous aqueous
dispersion.
[0299]In some embodiments, the drug powders for aqueous dispersion
described herein comprise size stabilized drug particles having an
effective particle size by weight of less than 500 nm formulated with
drug particles having an effective particle size by weight of greater
than 500 nm. In certain embodiments, the formulations have a particle
size distribution wherein about 10% to about 100% of the drug particles
by weight are between about 75 nm and about 500 nm, about 0% to about 90%
of the drug particles by weight are between about 150 nm and about 400
nm, and about 0% to about 30% of the drug particles by weight are greater
than about 600 nm. The drug particles described herein can be amorphous,
semi-amorphous, crystalline, semi-crystalline, or mixture thereof.
[0300]In one embodiment, the aqueous suspensions or dispersions described
herein comprise drug particles or drug complex at a concentration of
about 20 mg/ml to about 150 mg/ml of suspension. In another embodiment,
the aqueous oral dispersions described herein comprise drug particles or
drug complex particles at a concentration of about 25 mg/ml to about 75
mg/ml of solution. In yet another embodiment, the aqueous oral
dispersions described herein comprise drug particles or drug complex at a
concentration of about 50 mg/ml of suspension. The aqueous dispersions
described herein are especially beneficial for the administration of drug
to infants (less than 2 years old), children under 10 years of age and
any patient group that is unable to swallow or ingest solid oral dosage
forms.
[0301]Liquid drug formulation dosage forms for oral administration can be
aqueous suspensions selected from the group including, but not limited
to, pharmaceutically acceptable aqueous oral dispersions, emulsions,
solutions, and syrups. See, e.g., Singh et al., Encyclopedia of
Pharmaceutical Technology, 2.sup.nd Ed., pp. 754-757 (2002). In addition
to drug particles, the liquid dosage forms may comprise additives, such
as: (a) disintegrating agents; (b) dispersing agents; (c) wetting agents;
(d) at least one preservative, (e) viscosity enhancing agents, (f) at
least one sweetening agent, (g) at least one flavoring agent, and (h) a
complexing agent. In some embodiments, the aqueous dispersions can
further comprise a crystalline inhibitor.
[0302]Examples of disintegrating agents for use in the aqueous suspensions
and dispersions include, but are not limited to, a starch, e.g., a
natural starch such as corn starch or potato starch, a pregelatinized
starch such as National 1551 or Amijel.RTM., or sodium starch glycolate
such as Promogel.RTM. or Explotab.RTM.; a cellulose such as a wood
product, microcrystalline cellulose, e.g., Avicel.RTM., Avicel.RTM.
PH101, Avicel.RTM. PH102, Avicel.RTM. PH105, Elcema.RTM. P100,
Emcocel.RTM., Vivacel.RTM., Ming Tia.RTM., and Solka-Floc.RTM.,
methylcellulose, croscarmellose, or a cross-linked cellulose, such as
cross-linked sodium carboxymethylcellulose (Ac-Di-Sol.RTM.), cross-linked
carboxymethylcellulose, or cross-linked croscarmellose; a cross-linked
starch such as sodium starch glycolate; a cross-linked polymer such as
crosspovidone; a cross-linked polyvinylpyrrolidone; alginate such as
alginic acid or a salt of alginic acid such as sodium alginate; a clay
such as Veegum.RTM. HV (magnesium aluminum silicate); a gum such as agar,
guar, locust bean, Karaya, pectin, or tragacanth; sodium starch
glycolate; bentonite; a natural sponge; a surfactant; a resin such as a
cation-exchange resin; citrus pulp; sodium lauryl sulfate; sodium lauryl
sulfate in combination starch; and the like.
[0303]Dispersing/suspending agents and/or viscosity modulating agents
include materials that control the diffusion and homogeneity of a drug
through liquid media or a granulation method or blend method. In some
embodiments, these agents also facilitate the effectiveness of a coating
or eroding matrix. Viscosity enhancing agents are agents which are
typically added to a particulate dispersion to increase the viscosity and
prevent or slow settling of the particles. Viscosity enhancing agents in
solid dosage forms are used on occasion to form a gel matrix as water
permeates the solid dosage form and can delay the release of the
pharmaceutically active ingredient(s). In some embodiments, the
dispersing agents suitable for the aqueous suspensions and dispersions
described herein are known in the art and include, for example,
hydrophilic polymers, electrolytes, Tween.RTM. 60 or 80, PEG,
polyvinylpyrrolidone (PVP; commercially known as Plasdone.RTM.), and the
carbohydrate-based dispersing agents such as, for example,
hydroxypropylcellulose and hydroxypropylcellulose ethers (e.g., HPC,
HPC-SL, and HPC-L), hydroxypropylmethylcellulose and
hydroxypropylmethylcellulose ethers (e.g. HPMC K100, HPMC K4M, HPMC K15M,
and HPMC K100M), carboxymethylcellulose sodium, methylcellulose,
hydroxyethylcellulose, hydroxypropylmethylcellulose phthalate,
hydroxypropylmethylcellulose acetate stearate, noncrystalline cellulose,
magnesium aluminum silicate, triethanolamine, polyvinyl alcohol (PVA),
polyvinylpyrrolidone/vinyl acetate copolymer (Plasdone.RTM., e.g.,
S-630), 4-(1,1,3,3-tetramethylbutyl)-phenol polymer with ethylene oxide
and formaldehyde (also known as tyloxapol), poloxamers (e.g., Pluronics
F68.RTM., F88.RTM., and F108.RTM., which are block copolymers of ethylene
oxide and propylene oxide); and poloxamines (e.g., Tetronic 908.RTM.,
also known as Poloxamine 908.RTM., which is a tetrafunctional block
copolymer derived from sequential addition of propylene oxide and
ethylene oxide to ethylenediamine (BASF Corporation, Parsippany, N.J.)).
In other embodiments, the dispersing agent is selected from a group
comprising one of the following agents: hydrophilic polymers;
electrolytes; Tween.RTM. 60 or 80; PEG; polyvinylpyrrolidone (PVP);
hydroxypropylcellulose and hydroxypropyl cellulose ethers (e.g., HPC,
HPC-SL, and HPC-L); hydroxypropyl methylcellulose and hydroxypropyl
methylcellulose ethers (e.g. HPMC K100, HPMC K4M, HPMC K15M, HPMC K100M,
and Pharmacoat.RTM. 603 (Shin-Etsu)); carboxymethylcellulose sodium;
methylcellulose; hydroxyethylcellulose; hydroxypropylmethyl-cellulose
phthalate; hydroxypropylmethyl-cellulose acetate stearate;
non-crystalline cellulose; magnesium aluminum silicate; triethanolamine;
polyvinyl alcohol (PVA); 4-(1,1,3,3-tetramethylbutyl)-phenol polymer with
ethylene oxide and formaldehyde; poloxamers (e.g., Pluronics F68.RTM.,
F88.RTM., and F108.RTM., which are block copolymers of ethylene oxide and
propylene oxide); or poloxamines (e.g., Tetronic 908.RTM., also known as
Poloxamine 908.RTM.).
[0304]Wetting agents (including surfactants) suitable for the aqueous
suspensions and dispersions described herein are known in the art and
include, but are not limited to, acetyl alcohol, glycerol monostearate,
polyoxyethylene sorbitan fatty acid esters (e.g., the commercially
available Tweens.RTM. such as e.g., Tween 20.RTM. and Tween 80.RTM. (ICI
Specialty Chemicals)), and polyethylene glycols (e.g., Carbowaxs
3350.RTM. and 1450.RTM., and Carpool 934.RTM. (Union Carbide)), oleic
acid, glyceryl monostearate, sorbitan monooleate, sorbitan monolaurate,
triethanolamine oleate, polyoxyethylene sorbitan monooleate,
polyoxyethylene sorbitan monolaurate, sodium oleate, sodium lauryl
sulfate, sodium docusate, triacetin, vitamin E TPGS, sodium taurocholate,
simethicone, phosp
hotidylcholine and the like.
[0305]Typically amounts of preservatives needed to pass anti-microbial
effectiveness testing as described by USP and EU methodology are used to
test appropriate preservative levels. Suitable preservatives for the
aqueous suspensions or dispersions described herein include, for example,
potassium sorbate, parabens (e.g., methylparaben and propylparaben) and
their salts, benzoic acid and its salts, other esters of
parahydroxybenzoic acid such as butylparaben, alcohols such as ethyl
alcohol or benzyl alcohol, phenolic compounds such as phenol, or
quaternary compounds such as benzalkonium chloride. Preservatives, as
used herein, are incorporated into the dosage form at a concentration
sufficient to inhibit microbial growth. In one embodiment, the aqueous
liquid dispersion can comprise methylparaben and propylparaben in a
concentration ranging from about 0.01% to about 0.3% methylparaben by
weight to the weight of the aqueous dispersion and 0.005% to 0.03%
propylparaben by weight to the total aqueous dispersion weight. In yet
another embodiment, the aqueous liquid dispersion can comprise
methylparaben 0.05 to about 0.1 weight % and propylparaben from 0.01-0.02
weight % of the aqueous dispersion. In yet another embodiment, the
aqueous liquid dispersion can comprise sodium benzoate 0.05 to about 0.1
weight % of the aqueous dispersion and pH adjusted from 3.5 to 5.0.
[0306]Suspensions or dispersions described herein include, but are not
limited to, methyl cellulose, xanthan gum, carboxymethylcellulose,
hydroxypropyl cellulose, hydroxypropylmethyl cellulose, Plasdone.RTM.
S-630, carbomer, polyvinyl alcohol, alginates, acacia, chitosans and
combinations thereof. The concentration of the viscosity enhancing agent
will depend upon the agent selected and the viscosity desired.
[0307]Examples of natural and artificial sweetening agents suitable for
the aqueous suspensions or dispersions described herein include, for
example, acacia syrup, acesulfame K, alitame, anise, apple, aspartame,
banana, Bavarian cream, berry, black currant, butterscotch, calcium
citrate, camphor, caramel, cherry, cherry cream, chocolate, cinnamon,
bubble gum, citrus, citrus punch, citrus cream, cotton candy, cocoa,
cola, cool cherry, cool citrus, cyclamate, cylamate, dextrose,
eucalyptus, eugenol, fructose, fruit punch, ginger, glycyrrhetinate,
glycyrrhiza (licorice) syrup, grape, grapefruit, honey, isomalt, lemon,
lime, lemon cream, monoammonium glyrrhizinate (MagnaSweet.RTM.), maltol,
mannitol, maple, marshmallow, menthol, mint cream, mixed berry,
neohesperidine DC, neotame, orange, pear, peach, peppermint, peppermint
cream, Prosweet.RTM. Powder, raspberry, root beer, rum, saccharin,
safrole, sorbitol, spearmint, spearmint cream, strawberry, strawberry
cream, stevia, sucralose, sucrose, sodium saccharin, saccharin,
aspartame, acesulfame potassium, mannitol, talin, sucralose, sorbitol,
Swiss cream, tagatose, tangerine, thaumatin, tutti fruitti, vanilla,
walnut, watermelon, wild cherry, wintergreen, xylitol, or any combination
of these flavoring ingredients, e.g., anise-menthol, cherry-anise,
cinnamon-orange, cherry-cinnamon, chocolate-mint, honey-lemon,
lemon-lime, lemon-mint, menthol-eucalyptus, orange-cream, vanilla-mint,
and mixtures thereof. In one embodiment, the aqueous liquid dispersion
can comprise a sweetening agent or flavoring agent in a concentration
ranging from about 0.0001% to about 10.0% the weight of the aqueous
dispersion. In another embodiment, the aqueous liquid dispersion can
comprise a sweetening agent or flavoring agent in a concentration ranging
from about 0.0005% to about 5.0 wt % of the aqueous dispersion. In yet
another embodiment, the aqueous liquid dispersion can comprise a
sweetening agent or flavoring agent in a concentration ranging from about
0.0001% to 0.1 wt %, from about 0.001% to about 0.01 weight %, or from
0.0005% to 0.004% of the aqueous dispersion.
[0308]In addition to the additives listed above, the liquid drug
formulations can also comprise inert diluents commonly used in the art,
such as water or other solvents, solubilizing agents, and emulsifiers.
[0309]In certain embodiments, the invention is directed to an oral liquid
dosage form comprising from about 2.5% to about 5% size stabilized drug
complex particles, from about 2% to about 5% hydroxypropylmethyl
cellulose, about 0.5% to about 1.5% polyvinyl alcohol, from about 0.1% to
about 0.3% sodium lauryl sulfate, from about 0.005% to about 0.02%
simethicone, from about 0.01% to about 0.03% sucralose, from about 0.05%
to about 0.1% methylparaben, from about 0.01% to about 0.02%
propylparaben, from about 0.05 to about 0.1% sodium benzoate, from about
0.05% to about 0.15% citric acid, from about 0.005 to about 0.1% sodium
citrate and from about 0.002% to about 0.004% flavoring, the liquid
having a pH of about 3.8 to about 4.2, wherein all percentages are weight
percent to the total liquid formulation weight.
[0310]In certain embodiments, the invention is directed to an oral liquid
dosage form comprising size stabilized complexed drug particles and at
least one pharmaceutically acceptable excipient, the particles suspended
in a pharmaceutically acceptable liquid vehicle, wherein the volume
weighted median diameter (D50) after a suitable curing time does not
change by more than about 15% after 10 days storage at room temperature,
by more than about 12% after 10 days storage at room temperature, by more
than about 10% after 10 days storage at room temperature, by more than
about 8% after 10 days storage at room temperature, by more than about
15% after 20 days of storage at room temperature, by more than about 15%
after 40 days of storage at room temperature, by more than about 15%
after 60 days of storage at room temperature, or by more than about 15%
after 80 days of storage at room temperature. In certain aspects, the
volume weighted median diameter (D50) of the size stabilized drug complex
particles prior to storage is from about 100 nm to about 500 nm, or from
about 100 nm to about 350 nm.
[0311]In certain embodiments, the invention is directed to an oral liquid
dosage form wherein the volume weighted median diameter (D50) of the size
stabilized drug complex particles do not change by more than about 15%
when placed in a glass vial and heated in a 100.degree. C. oil bath for
20 minutes, does not change by more than about 15% when placed in a glass
vial and heated in a 100.degree. C. oil bath for 4 hours, does not change
by more than about 10% when placed in a glass vial and heated in a
100.degree. C. oil bath for 20 minutes, does not change by more than
about 5% when placed in a glass vial and heated in a 100.degree. C. oil
bath for 20 minutes, or does not change when placed in a glass vial and
heated in a 100.degree. C. oil bath for 20 minutes (within the accuracy
of the particle size measurement procedure).
[0312]In still further embodiments, the invention is directed to an oral
liquid dosage form the volume weighted median diameter (D50) of the size
stabilized drug complex particles does not change by more than about 25%
when placed in a HDPE container and frozen and thawed three or more times
with the time frozen for each cycle being at least 12 hours. The frozen
temperature can be any suitable freezing temperature, e.g., from about
-80.degree. C. to about -20.degree. C.
[0313]In certain embodiments, the oral liquid dosage form is prepared by
contacting drug particles with a complexing agent, wherein the size of
the particles exhibits an increase in volume weighted median diameter
(D50) of from about 20% to about 300% and reaching an endpoint such that
the particles are size stabilized.
[0314]In certain solid formulations, the size stabilized drug complex
particles are dispersed in a liquid to form a suspension and the
suspension is spray coated onto the plurality of substrates, or spray
granulated with the plurality of substrates. In further embodiments the
drug particles are dispersed in a liquid to form a suspension and the
suspension is spray dried to form a powder which is then granulated and
added to a capsule or granulated and compressed into a tablet. The
suspension can be, e.g., about 5% to about 35%, or about 15% to about 25%
total solids. The drug concentration in the solids can be, e.g., from
about 20% to about 80%.
[0315]In embodiments directed to liquid dosage forms, the liquid dosage
form can include at least one excipient selected from
hydroxypropylmethylcellulose, sodium lauryl sulfate, methyl anthranilate,
sodium benzoate, citric acid, sodium citrate, simethicone, sucralose and
flavoring. For example, the liquid dosage form can comprise about 5%
drug, about 5% hydroxypropylmethylcellulose (2910), about 0.1% sodium
lauryl sulfate, about 0.4% methylanthranilate about 0.1% sodium benzoate,
about 0.12% citric acid, about 0.06% sodium citrate, about 0.01%
simethicone, and 0.02% sucralose. These ingredients and % amounts are not
meant to be limiting.
Emulsions
[0316]In some embodiments, the pharmaceutical drug formulations described
herein can be self-emulsifying drug delivery systems (SEDDS). Emulsions
are dispersions of one immiscible phase in another, usually in the form
of droplets. Generally, emulsions are created by vigorous mechanical
dispersion. SEDDS, as opposed to emulsions or microemulsions,
spontaneously form emulsions when added to an excess of water without any
external mechanical dispersion or agitation. An advantage of SEDDS is
that only gentle mixing is required to distribute the droplets throughout
the solution. Additionally, water or the aqueous phase can be added just
prior to administration, which ensures stability of an unstable or
hydrophobic active ingredient. Thus, the SEDDS provides an effective
delivery system for oral and parenteral delivery of hydrophobic active
ingredients. SEDDS may provide improvements in the bioavailability of
hydrophobic active ingredients. Methods of producing self-emulsifying
dosage forms are known in the art include, but are not limited to, for
example, U.S. Pat. Nos. 5,858,401, 6,667,048, and 6,960,563, each of
which is specifically incorporated by reference.
[0317]Exemplary emulsifiers are ethyl alcohol, isopropyl alcohol, ethyl
carbonate, ethyl acetate, benzyl alcohol, benzyl benzoate, propylene
glycol, 1,3-butyleneglycol, dimethylformamide, sodium lauryl sulfate,
sodium doccusate, cholesterol, cholesterol esters, taurocholic acid,
phosp
hotidylcholine, oils, such as cottonseed oil, groundnut oil, corn
germ oil, olive oil, castor oil, and sesame oil, glycerol,
tetrahydrofurfuryl alcohol, polyethylene glycols, fatty acid esters of
sorbitan, or mixtures of these substances, and the like.
Intranasal Formulations
[0318]Intranasal formulations are known in the art and are described in,
for example, U.S. Pat. Nos. 4,476,116, 5,116,817 and 6,391,452, each of
which is specifically incorporated by reference. Drug formulations
prepared according to these and other techniques well-known in the art
are prepared as solutions in saline, employing benzyl alcohol or other
suitable preservatives, fluorocarbons, and/or other solubilizing or
dispersing agents known in the art. See, for example, Ansel, H. C. et
al., Pharmaceutical Dosage Forms and Drug Delivery Systems, Sixth Ed.
(1995). Preferably these compositions and formulations are prepared with
suitable nontoxic pharmaceutically acceptable ingredients. These
ingredients are known to those skilled in the preparation of nasal dosage
forms and some of these can be found in REMINGTON: THE SCIENCE AND
PRACTICE OF PHARMACY, 21st edition, 2005, a standard reference in the
field. The choice of suitable carriers is highly dependent upon the exact
nature of the nasal dosage form desired, e.g., solutions, suspensions,
ointments, or gels. Nasal dosage forms generally contain large amounts of
water in addition to the active ingredient. Minor amounts of other
ingredients such as pH adjusters, emulsifiers or dispersing agents,
preservatives, surfactants, gelling agents, complexing agents or
buffering and other stabilizing and solubilizing agents may also be
present. Preferably, the nasal dosage form should be isotonic with nasal
secretions.
Buccal Formulations
[0319]Buccal formulations comprising the drug formulations described
herein may be administered using a variety of formulations known in the
art. For example, such formulations include, but are not limited to, U.S.
Pat. Nos. 4,229,447, 4,596,795, 4,755,386, and 5,739,136, each of which
is specifically incorporated by reference. In addition, the buccal dosage
forms described herein can further comprise a bioerodible (hydrolyzable)
polymeric carrier that may also serves to adhere the dosage form to the
buccal mucosa. The buccal dosage form is fabricated so as to erode
gradually over a predetermined time period, wherein drug delivery is
provided essentially throughout. Buccal drug delivery, as will be
appreciated by those skilled in the art, avoids the disadvantages
encountered with oral drug administration, e.g., slow drug absorption,
degradation of the active agent by fluids present in the gastrointestinal
tract and/or first-pass inactivation in the liver. With regard to the
bioerodible (hydrolysable) polymeric carrier, it will be appreciated that
virtually any such carrier can be used, so long as the desired drug
release profile is not comprised, and the carrier is compatible with drug
and any other components that may be present in the buccal dosage unit.
Generally, the polymeric carrier comprises hydrophilic (water-soluble and
water-swellable) polymers that adhere to the wet surface of the buccal
mucosa. Examples of polymeric carriers useful herein include acrylic acid
polymers e.g., those known as "carbomers" (Carbopol.RTM., which may be
obtained from B.F. Goodrich, is one such polymer). Other components may
also be incorporated into the buccal dosage forms described herein
include, but are not limited to, disintegrants, diluents, binders,
lubricants, flavoring, colorants, preservatives, and the like.
Transdermal Formulations
[0320]Transdermal formulations described herein may be administered using
a variety of devices which have been described in the art. For example,
such devices include, but are not limited to, U.S. Pat. Nos. 3,598,122,
3,598,123, 3,710,795, 3,731,683, 3,742,951, 3,814,097, 3,921,636,
3,972,995, 3,993,072, 3,993,073, 3,996,934, 4,031,894, 4,060,084,
4,069,307, 4,077,407, 4,201,211, 4,230,105, 4,292,299, 4,292,303,
5,336,168, 5,665,378, 5,837,280, 5,869,090, 6,923,983, 6,929,801 and
6,946,144, each of which is specifically incorporated by reference in its
entirety. In some embodiments, the transdermal delivery device used with
the drug formulations described herein can comprise a power source, radio
frequency, or a brief electrical current to micro-electrodes in the skin
creating "channels" or "pores" in the stratum corneum to facilitate the
delivery of the drug formulation, such methods are known in the art and
are described in, for example U.S. Pat. Nos. 6,611,706, 6,708,060, and
6,711,435, each of which is specifically incorporated by reference in its
entirety. In other embodiments, the transdermal delivery device can
comprise a means for porating the stratum corneum, e.g., micro-lancing,
application of sonic energy, or hydraulic puncturing, to facilitate the
delivery of the drug formulation, such methods are known in the art and
are described in, for example, U.S. Pat. Nos. 6,142,939 and 6,527,716,
each of which is specifically incorporated by reference in its entirety.
The pores described by the methods herein are typically about 20-50
microns in depth and do not extend into areas of innervation or
vascularization.
[0321]The transdermal dosage forms described herein may incorporate
certain pharmaceutically acceptable excipients which are conventional in
the art. In general, the transdermal formulations described herein
comprise at least three components: (1) a drug complex formulation; (2) a
penetration enhancer; and (3) an aqueous adjuvant. In addition,
transdermal formulations can include additional components such as, but
not limited to, gelling agents, creams and ointment bases, and the like.
In some embodiments, the transdermal formulation can further comprise a
woven or non-woven backing material to enhance drug absorption and
prevent the removal of the transdermal formulation from the skin. In
other embodiments, the transdermal formulations described herein can
maintain a saturated or supersaturated state to promote diffusion into
the skin.
Injectable Formulations
[0322]Size stabilized drug complex formulations suitable for
intramuscular, subcutaneous, or intravenous injection may comprise
physiologically acceptable sterile aqueous or non-aqueous solutions,
dispersions, suspensions or emulsions, and sterile powders for
reconstitution into sterile injectable solutions or dispersions. Examples
of suitable aqueous and non-aqueous carriers, diluents, solvents, or
vehicles including water, ethanol, polyols (propylene glycol,
polyethylene-glycol, glycerol, cremophor and the like), suitable mixtures
thereof, vegetable oils (such as olive oil) and injectable organic esters
such as ethyl oleate. Proper fluidity can be maintained, for example, by
the use of a coating such as lecithin, by the maintenance of the required
particle size in the case of dispersions, and by the use of surfactants.
Drug formulations suitable for subcutaneous injection may also contain
additives such as preserving, wetting, emulsifying, and dispensing
agents. Prevention of the growth of microorganisms can be ensured by
various antibacterial and antifungal agents, such as parabens, benzoic
acid, benzyl alcohol, chlorobutanol, phenol, sorbic acid, and the like.
It may also be desirable to include isotonic agents, such as sugars,
sodium chloride, and the like. Prolonged drug absorption of the
injectable pharmaceutical form can be brought about by the use of agents
delaying absorption, such as aluminum monostearate and gelatin. Drug
suspension formulations designed for extended release via subcutaneous or
intramuscular injection can avoid first pass metabolism and lower dosages
of drug will be necessary to maintain plasma levels in therapeutic range.
In such formulations, the particle size of the drug particles and the
range of the particle sizes of the drug particles can be used to control
the release of the drug by controlling the rate of dissolution in fat or
muscle.
Sterile Drug Formulations
[0323]Some of the drug formulations described herein can be sterile
filtered. This property obviates the need for heat sterilization, which
can harm or degrade drug, as well as result effective particle size
growth.
[0324]Sterile filtration can be difficult because of the required small
particle size of the composition. However, this method is suitable and
commonly used for dispersions comprising nanoparticles. Filtration is an
effective method for sterilizing homogeneous solutions when the membrane
filter pore size is less than or equal to about 0.2 microns (200 nm)
because a 0.2 micron filter is sufficient to remove essentially all
bacteria. Sterile filtration is normally not used to sterilize
conventional suspensions of micron-sized drug because the drug particles
are too large to pass through the membrane pores.
[0325]Because some of the size stabilized drug-complex formulations
described herein can be sterilized via autoclaving, and because the
formulations can have a very small drug effective average particle size,
some sterilized drug formulations are suitable for parenteral
administration. Additionally, a sterile drug formulation is particularly
useful in treating immunocompromised patients, infants or juvenile
patients, patients with head trauma and the elderly.
Combination Therapies
[0326]The compositions and methods described herein may also be used in
conjunction with other well known therapeutic reagents that are selected
for their particular usefulness against the condition that is being
treated. In general, the compositions described herein and, in
embodiments where combinational therapy is employed, other agents do not
have to be administered in the same pharmaceutical composition, and may,
because of different physical and chemical characteristics, have to be
administered by different routes. The determination of the mode of
administration and the advisability of administration, where possible, in
the same pharmaceutical composition, is well within the knowledge of the
skilled clinician. The initial administration can be made according to
established protocols known in the art, and then, based upon the observed
effects, the dosage, modes of administration and times of administration
can be modified by the skilled clinician.
[0327]The particular choice of compounds used will depend upon the
diagnosis of the attending physicians and their judgment of the condition
of the patient and the appropriate treatment protocol. The compounds may
be administered concurrently (e.g., simultaneously, essentially
simultaneously or within the same treatment protocol) or sequentially,
depending upon the nature of the proliferative disease, the condition of
the patient, and the actual choice of compounds used. The determination
of the order of administration, and the number of repetitions of
administration of each therapeutic agent during a treatment protocol, is
well within the knowledge of the skilled physician after evaluation of
the disease being treated and the condition of the patient.
[0328]It is understood that the dosage regimen to treat, prevent, or
ameliorate the condition(s) for which relief is sought, can be modified
in accordance with a variety of factors. These factors include the
disorder from which the subject suffers, as well as the age, weight, sex,
diet, and medical condition of the subject. Thus, the dosage regimen
actually employed can vary widely and therefore can deviate from the
dosage regimens set forth herein.
[0329]The pharmaceutical agents which make up the combination therapy
disclosed herein may be a combined dosage form or in separate dosage
forms intended for substantially simultaneous administration. The
pharmaceutical agents that make up the combination therapy may also be
administered sequentially, with either therapeutic compound being
administered by a regimen calling for two-step administration. The
two-step administration regimen may call for sequential administration of
the active agents or spaced-apart administration of the separate active
agents. The time period between the multiple administration steps may
range from, a few minutes to several hours, depending upon the properties
of each pharmaceutical agent, such as potency, solubility,
bioavailability, plasma half-life and kinetic profile of the
pharmaceutical agent. Circadian variation of the target molecule
concentration may also determine the optimal dose interval.
[0330]In some embodiments, the drug formulation is administered with at
least one other agent, e.g., an anti-convulsant agent, an anti-anxiety
agent or an anti-depression agent.
Controlled Exposure Profiles
[0331]In certain embodiments, about 40% of the drug is released from the
dosage form within about 3 hours and about 95% of the drug is released
from the dosage form within about 10 hours after administration. In yet
another embodiment, about 30% of the drug is released from the dosage
form within about 3 hours and about 90% of the drug is released from the
dosage form within about 10 hours after administration. In yet another
embodiment, about 80% of the drug is released from the dosage form within
about 2 hours and about 90% of the drug is released from the dosage form
within about 10 hours after administration.
Reduced Fed/Fasted Effects Associated with the Administration of Drug
[0332]It is generally known in the art that if a positive fed/fasted
effect is seen with a pharmaceutical agent, it is typically related to
the dose of the active agent administered such that a lower dose of an
active agent will have a lower ratio of AUC.sub.(fed)/AUC.sub.(fasted)
and a higher dose of an active agent will have a higher ratio of
AUC.sub.(fed)/AUC.sub.(fasted). In addition, it is known that dosage
forms which substantially eliminate the effects of food on the
therapeutic window (levels for efficacy vs. levels giving side effects)
are safer than those dosage forms which do not. Thus dosage forms that
provide reduced fed/fasted effects provide decreased risks and reduce the
potential for side effects, thereby increasing subject safety and
compliance. Fed/fasted conditions are in accordance with FDA guidelines
for testing drug exposure in the fed and fasted states.
[0333]Conventional formulations of drug display large fed/fasted effects
in a manner that is not limited to dose dependency. The drug formulations
described herein are less effected by the fed or fasted state of the
subject being administered the formulation. The systemic exposure of the
drug formulations described herein is less sensitive to the type of meal
ingested than conventional drug formulations. This means that there is a
reduced difference in the AUC.sub.(0-.tau.) values of drug when the drug
formulations are administered in the fed versus the fasted state at
therapeutically effective doses. Thus, described herein are drug
formulations that can substantially reduce the effect of food on the
pharmacokinetics of drug. In one embodiment, the drug formulation is an
aqueous dispersion that when administered to a child under 12 yeas old or
adult not capable of swallowing a solid formulation, provides a ratio of
the AUC.sub.(0-.infin.) or AUC.sub.(0-.tau.) values of drug, when
administered in the fed versus the fasted state, of less than about 4. In
another embodiment, the drug formulation is a solid oral dosage form that
when administered to a human over twelve years old provides a the ratio
of the AUC.sub.(0-.tau.) values of drug, when administered in the fed
versus the fasted state, of less than about 3. In still another
embodiment, the drug formulation is a solid oral dosage form that when
administered to a human over twelve years old provides a ratio of the
AUC.sub.(0-.tau.) values of drug, when administered in the fed versus the
fasted state, of less than about 2. In yet another embodiment, the drug
formulation is a solid oral dosage form that when administered to a human
over twelve years old provides a ratio of the AUC.sub.(0-.tau.) values of
drug, when administered in the fed versus the fasted state, of less than
about 1.5. In still another embodiment, the drug formulation is a solid
oral dosage form that when administered to a human over twelve years old
provides a ratio of the AUC.sub.(0-.tau.) values of drug, when
administered in the fed versus the fasted state, ranging from about 3 to
about 1.5. In another embodiment, the drug formulation is a solid oral
dosage form that when administered to a human over twelve years old
provides a ratio of the AUC.sub.(0-.tau.) values of drug, when
administered in the fed versus the fasted state, of about 2.
Dose Amounts
[0334]The drug formulations described herein are administered and dosed in
accordance with good medical practice, taking into account the clinical
condition of the individual patient, the site and method of
administration, scheduling of administration, and other factors known to
medical practitioners. In human therapy, the dosage forms described
herein preferably deliver drug formulations that maintain a
therapeutically effective amount of drug at steady state while reducing
the side effects associated with an elevated C.sub.max blood plasma level
of drug.
[0335]In various other embodiments of the present invention, the amount of
drug administered to a subject via a solid dosage form is the amount
known in the art to achieve a therapeutically effective concentration of
drug in the bloodstream of a human or animal in need thereof. For
example, the amount of drug may range from about 0.01 micrograms to about
6 g. In other embodiments, the amount of drug may range from about 0.1 mg
to about 1000 mg. In other embodiments, the amount of drug may range from
about 1 mg to about 500 mg, from about 50 mg to about 800 mg or from
about 300 mg to about 700 mg. In one embodiment, a drug formulation is
administered in a solid dosage form at a concentration of about 250 mg to
about 650 mg. In another embodiment, the drug formulation is administered
in a solid dosage form at concentration of about 300-400 mg. In another
aspect, the solid oral dosage form can be administered twice a day
(b.i.d). In yet another aspect, the solid oral dosage form is a
controlled release dosage form administered b.i.d. providing a pulsatile
release of drug such that the C.sub.max of blood plasma drug is reduced
to avoid adverse effects while simultaneously reducing fed/fasted effects
and maintaining total exposure (AUC.sub.(0-.infin.)).
[0336]A therapeutically effective concentration of an oral aqueous
suspension or dispersion comprising a drug formulation described herein,
administered according to the methods described herein, is typically in
the range of about 20 mg/ml to about 150 mg/ml final concentration. In
one embodiment, a drug formulation is administered as an aqueous oral
suspension at a concentration of about 25 mg/ml to about 100 mg/ml final
concentration. In another embodiment, a drug formulation is administered
as an aqueous oral suspension at a concentration of about 50 mg/ml final
concentration. The aqueous oral suspensions comprising a drug formulation
described herein can be administered both as a single dose per day or
given multiple times within a 24 hour period. In one aspect, the aqueous
oral suspension can be administered three times a day (t.i.d). In another
aspect, the aqueous oral suspension can be administered twice a day
(b.i.d.).
[0337]Contemplated compositions of the present invention provide a
therapeutically effective amount of drug over an interval of about 30
minutes to about 8 hours after administration, enabling, for example,
once-a-day, twice-a-day, three times a day, and etc. administration if
desired.
[0338]In further embodiments, greater than about 95%; or greater than
about 90%; or greater than about 80%; or greater than about 70% of the
drug dosed by weight is absorbed into the bloodstream within 8 hours
after administration.
[0339]In other embodiments, the pharmaceutical formulations provide a
release profile for an immediate release dosage form of the drug, whereby
using methods described in Example 29, whereby about 80% (or about 70% or
about 90%) of the drug is released from the dosage form within about 1
hours in SGF and for a delayed release drug dosage form about 60% of the
(or preferably 70% or 80%) is released from the composition within about
3 hours in SIF.
Pharmacokinetic Analysis
[0340]Plasma concentrations of drug referenced herein are intended to mean
total drug concentrations including both free and bound drug. Any
formulation giving the desired pharmacokinetic profile is suitable for
administration according to the present methods. Exemplary types of
formulations giving such profiles are liquid dispersions and solid dose
forms of the drug formulation described herein. Aqueous dispersions of
drug are size stable at temperatures from 4.degree. C. to 40.degree. C.
for at least 4 months.
[0341]Certain drug compositions and formulations described herein display
enhanced pharmacokinetic (PK) and pharmacodynamic (PD) profiles and/or
minimized side effects as compared to conventional drug formulations
known in the art.
[0342]Certain formulations described herein reduce the risk of drug side
effects (e.g., ataxia, sedation and somnolence) relative to conventional
drug formulations. In certain embodiments improved performance compared
to conventional drug formulations can be seen on acute doses. In other
embodiments, maximal benefit of the drug formulations described herein
can be seen at steady state.
[0343]Any hypotheses provided herein are for possible explanatory purposes
only, and is not meant to be limiting in any way with respect to the
appended claims. All U.S. patent references discussed in the
specification are hereby incorporated by reference.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
[0344]This invention is further illustrated by the following examples that
should not be construed as limiting. Those of skill in the art of
pharmaceutical formulation will readily appreciate that certain
modifications to the examples described herein may be needed,
particularly for changes in formulation batch size. Any methods,
materials, or excipients which are not particularly described will be
generally known and available to those skilled in the drug design and
assay and pharmacokinetic analysis.
[0345]The particle size data, for examples in which a ganaxolone or
phenyloin particle size is reported, were obtained using a Horiba LA-910
Laser Light Scattering Particle Size analyzer (Horiba Instruments,
Irvine, Calif.) and reported as volume weighted median (D50). Studies of
ganaxolone or phenyloin particles in liquids, beads, powders and
immediate release dosage forms in SGF and SIF are performed by dispersing
an appropriate amount of the ganaxolone or phenyloin formulation into 20
mL (unless otherwise specified) of SGF or SIF in a vial to obtain a
measuring concentration of ganaxolone or phenyloin of about 0.5 mg/mL.
For example, in one embodiment, 200 mg of a ganaxolone suspension
formulation containing 5 wt % of ganaxolone and appropriate levels of
HPMC, PVA, SLS, and complexing agents was dispersed into 20 mL of SGF or
SIF in a vial for measurement. The vial is immersed in an oil bath kept
at 36 to 38.degree. C. for 3 h. The sample is assessed visually for signs
of flocculation and particle size is measured on a Horiba LA-910 to
obtain D50 values.
[0346]Compositions/formulations are expressed weight percent (% wt) of the
total composition for liquid suspensions and as weight percent (% wt) to
the drug (API) for solid compositions unless specified otherwise.
Abbreviations
[0347]The following abbreviations are used in the examples below. Other
abbreviations used in the examples will be understood by those of skill
in the art of pharmaceutical formulations.
GNX Ganaxolone
HDPE High Density Polyethylene
HPMC Hydroxypropylmethylcellulose-2910
[0348]PVA Polyvinyl alcohol (USP)
SLS Sodium Lauryl Sulfate
[0349]DOSS Sodium docusateSGF Simulated gastric fluid USP without
enzymeSIF Simulated intestinal fluid USP without enzyme
WT Weight
[0350]rt room temperatureD50 Volume weighted median particle size
MCC Microcrystalline Cellulose
API Active Pharmaceutical Ingredient
[0351]DI water: Deionized water
Example 1
Preparation of USP Simulated Gastric and Intestinal Fluid
Simulated Intestinal Fluid (SIF)
[0352]Monobasic potassium phosphate (6.8 g) and sodium hydroxide (0.616 g)
are added into 250 ml of distilled water in a 1000 ml volumetric flask
and swirled until dissolved. 700 ml distilled water is added and the pH
checked. The pH is adjusted to pH 6.8+/-0.1 by adding either 0.2N sodium
hydroxide or 0.2N hydrochloric acid and the volume is brought to 1000 ml.
Simulated Gastric Fluid (SGF)
[0353]Sodium chloride (2 g), 750 ml distilled water, and 7.0 ml of
concentrated hydrochloric acid are added into a 1000 ml volumetric flask.
The flask is swirled to mix and the volume brought to 1000 ml with
distilled water. The pH should be approx. 1.2.
Example 2
Particle Size Measurement Method
[0354]The following methods and settings for particle size measurement
were used for all D50 values for ganaxolone and phenyloin.
Particle Size Method Using Horiba Laser Scattering Particle Size
Distribution Analyzer LA-910
[0355]Particle size measurement using Horiba laser scattering particle
size distribution analyzer is generally well known for those skilled in
the art. It is important that the parameters be kept constant when
measuring different samples if they are used for comparison purposes. For
ganaxolone and phenyloin nanoparticulate compositions, instrument
settings and sample preparation method are described below:
Instrument Settings and Parameters:
[0356]Measure Conditions: Circulation=4; ultrasonic time=1; agitation=1;
sampling times: red laser=10, blue lamp=2; preferred % transmittance:
blue lamp=75-80%; blank: red laser=10, blue lamp=2. For D50 values after
sonication, the sonication power is set to low and the sonication time is
1 minute.
[0357]Display Settings:
[0358]Form of distribution: standard (Gaussian)=10 iterations; RR
Index=1.15-010; distribution base: volume; size class=passing
(underclass).
Example 2A
Sample Preparation and Particle Size (D50) Determination
[0359]For concentrated nanoparticle drug suspensions, dilute the
nanoparticulate composition with deionized water to approximately 5 mg/mL
API concentration. Shake well for 15-30 seconds. Add 120 mL of deionized
water to the chamber, turn agitation and recirculation settings on.
Transfer the nanoparticulate suspension via a pipette to the sample
chamber in sufficient quantity to reach the transmittance range of 75-80%
blue lamp. If a suspension or stability indicating dispersion is at a
concentration of approximately 0.5 mg/ml do not further dilute if not
necessary and use directly for particle size measurement. Transfer the
sample to be measured via a pipette to up to the desired transmittance
range (75-80% blue lamp). Take a measurement and collect the D50 value.
This will be the unsonicated particles size. Sonicate for 1 min and take
a measurement again to collect D50 value. This will be the particle size
after 1 minute sonication. One can also use this procedure obtain other
particle size parameters such as D10 or D90 values.
Example 2B
General Particle Size Method for Solid Formulations Containing Insoluble
Excipients
[0360]Use the following method if measuring formulations where insoluble
excipients are added: Calculate the amount of insoluble excipients that
will be present in the measurement of the composition and conduct the
particle size experiment using these insoluble excipients and the same
conditions as will be used in the measurement of D50 with the
composition. Blank the instrument and drain. Measure the particle size
(D50) of the composition as described above. This process subtracts any
particle size interference from the insoluble excipients. In the case
where the only insoluble excipient are MCC cores, pipette the dispersed
suspension (excluding MCC cores) to the Horiba chamber containing 120 ml
distilled water. Measure the particle size as per method 2A.
Examples 3A-B
Dispersion Testing
Example 3A
Dispersion Testing for Aggregation of Liquid and Solid Nanoparticulate
Compositions
[0361]General method: The solid or liquid nanoparticulate composition is
placed in a 25 ml HDPE vial with HDPE cap and is diluted with 15-20 ml of
simulated gastric or intestinal fluid to achieve a final API
concentration of approx 0.5 mg/ml. The vial is agitated manually for
until completely dispersed (generally 15-30 seconds). The vial is then
placed in a heated oil bath at 36-38.degree. C. unstirred unless
specified otherwise until the desired test time. The vial is removed from
the bath and inspected visually for signs of flocculation. After shaking
the contents of the vial for 15-30 seconds manually, the particle size is
determined (D50) using a Horiba-LA-910 particle analyzer as described in
Example 2. A comparison of D50 values (e.g. after and before addition to
SGF or SIF) is used to define the degree of particle aggregation or
growth. Initial D50 values before addition to the dispersion media is
used as the initial for liquid compositions. Initial D50 value for a
solid composition is the D50 of the liquid composition prior to removal
of liquid (e.g. a spray suspension of API prior to spray drying, spray
granulation or spray layering).
Example 3B
[0362]Dispersion of Tablets and Capsules (Immediate and Delayed Release)
of Nanoparticulate Compositions
[0363]Place the drug solid dosage form in a type I (e.g, beads and
capsules) or type II (e.g., tablets) dissolution apparatus with basket at
36-38.degree. C. containing SGF at 0.5 to 1.0 mg/ml API concentration for
the immediate release component. Stir at 75 RPM and sample at 1 hour for
the particle size. Measure the particle size as described as Example 2.
For a controlled release dosage, follow the preparation above but
incubate in SGF for 2 hours, replace the SGF with SIF (0.5 to 1 mg/mL API
concentration) and incubate for an additional 3 hours. Measure the
particle size (D50) as described in Example 2.
Example 4
Preparation of Complexed Ganaxolone Nanoparticulate Compositions in the
Presence of a Complexing Agent
[0364]The purpose of this example is to show that the complexing agent can
be present during milling to obtain complexed ganaxolone nanoparticles.
[0365]Ganaxolone was wet milled in a 600 ml chamber using a DYNO-Mill KDL
equipped with four 64 mm polyurethane agitator discs. The mill was
operated at 3000 RPM or a tip speed of 10 m/sec. The mill was loaded with
88 vol % of 0.4 mm yttrium stabilized zirconium oxide beads. The milling
slurry (1200 g) contained 25 wt % ganaxolone (Marinus Pharmaceuticals
Inc., Connecticut, USA), 5 wt % hydroxypropyl methylcellulose (Pharmacoat
603), 0.0333 wt % 30% simethicone emulsion, 0.3 wt % sodium lauryl
sulfate and 0.2 wt % methylparaben. This slurry was circulated through
the mill via a peristaltic pump and returned to a cooled reservoir where
it was re-circulated through the mill. The mill was operated in this
recirculation mode, keeping the slurry temperature at 35-40.degree. C.,
for a total of 410 minutes (90 minutes residence time). The product
slurry was filtered through a 20 micron polypropylene cartridge filter.
The mill was flushed with 300 mL of the milling media (milling slurry
minus ganaxolone). The total weight of the milled slurry was 1185 g. The
concentration of ganaxolone was determined to be 20.5% by HPLC. The
particle size (D50) measured on a Horiba LA 910 was 0.164 .mu.m
unsonicated/0.153 .mu.m after 1 minute sonication. After 7 days at room
temperature, the particle size increased to 0.320 .mu.m
(unsonicated)/0.309 .mu.m (after 1 minute sonication). This formulation
was then used in different studies as described in other examples. The
D50 did not change by more than 10% after this curing period for the
duration of all other studies conducted with this formulation.
Examples 5A-C
Preparation of Ganaxolone Nanoparticulate Suspension without a Complexing
Agent
Example 5A
Residence Time 75 Minutes
[0366]The purpose of this example is to demonstrate preparation of an
aqueous ganaxolone dispersion without a complexing agent.
[0367]Ganaxolone milling slurry (1200 g) having the same composition as
described in Example 4 without methylparaben was milled as in Example 4
for 75 minutes of residence time. After filtration through a 20 micron
polypropylene cartridge filter and the mill was flushed with 300 mL of
milling media, milled ganaxolone slurry (1271 g) was obtained. The
concentration of ganaxolone was 21.25% by HPLC. The particle size (D50)
measured on a Horiba LA 910 was 0.103 .mu.m (unsonicated)/0.102 .mu.m
(after 1 min sonication). D50 increased slightly after storage under
refrigerated conditions. This formulation was used in other examples.
Example 5B
Residence Time 24 Minutes
[0368]Powdered ganaxolone aqueous dispersion (1200 g) comprising a mixture
of 30 wt % ganaxolone and 5 wt % HPMC, 0.2 wt % sodium lauryl sulfate and
100 ppm simethicone was milled in a DYNO Mill KDL as described for
Example 5A. After 24.0 minutes of residence time, D50 was 163 nm.
Example 5C
Residence Time 50.8 Minutes
[0369]Powdered ganaxolone aqueous dispersion (1200 g) comprising a mixture
of 15 wt % ganaxolone and 3 wt % HPMC was milled in a DYNO Mill KDL as
described for Example 5A. During milling, 2 portions of 0.05% w/w sodium
lauryl sulfate were added to keep the milling slurry fluid. After 50.8
minutes of residence time, D50 was 116 nm.
Example 6
Preparation of Uncomplexed Ganaxolone Nanoparticulate Suspension
Containing HPMC, SLS and Simethicone
[0370]Powdered ganaxolone aqueous dispersion (1500 g) comprising a mixture
of 25 wt % ganaxolone, 5 wt % HPMC, 0.1 wt % sodium lauryl sulfate and
0.028 wt % simethicone 30% emulsion (all based on total weight of the
dispersion in deionized water) was milled in a DYNO Mill KDL as described
in Example 5. After 43 minutes of residence time, the D50 was 0.113 .mu.m
(unsonicated)/0.112 (after 1 minute sonication). The final ganaxolone
concentration was 22.6% by HPLC. This formulation was used in Example 12.
Example 7
Preparation of Uncomplexed Ganaxolone Nanoparticulate Suspension
Containing HPMC and Sodium Lauryl Sulfate and Stability
[0371]Powdered ganaxolone in deionized water (180 g) containing a 30 wt %
ganaxolone (Marinus Pharmaceuticals Inc., Connecticut, USA), 3 wt % HPMC,
and 0.1% wt sodium lauryl sulfate (all based on total weight of
suspension) was milled in a DYNO Mill KDL (Willy A. Bachofen A. G.,
Maschinenfabrik, Basel, Switzerland) with a 300 mL glass batch chamber
and utilizing 0.1 mm zirconium oxide beads (260 mL, 85% of the chamber
volume). The milling was conducted for 120 min at a tip speed of 22.5
m/s. The particle size (D50) after milling was 0.106 .mu.m unsonicated.
The milled slurry (105 g) was diluted with 150 g of deionized water
containing 7 wt % HPMC and 0.1 wt % SLS to give a 15 wt % gnx suspension.
A sample of this 15 wt % slurry was further diluted using 100 g of the
slurry and 500 g of deionized water containing 5% HPMC and 0.1% SLS to
give a final concentration of 2.5% ganaxolone in 5% HPMC, 0.1% SLS and
water. The particle size (D50) remained unchanged at room temperature
(25.degree. C.) after 4 months. This ganaxolone nanoparticle suspension
underwent flocculation upon incubation in SGF and SIF (shown below) using
the method as described in Example 3. This material was used in one oral
dog pharmacokinetics study (Example 27, formulation 27A) to show
pharmacokinetics of an uncomplexed ganaxolone suspension (D50 of 110 nm)
which demonstrated good storage stability but aggregation in simulated
gastric and intestinal fluids.
TABLE-US-00001
Initial SGF 90 min SIF 90 min
D50 (.mu.m) unsonicated/ 0.110 0.390/0.118 0.535/0.134
1 min sonication
Visual observation Flocculation Flocculation
Example 8
Preparation of Uncomplexed Phenytoin Nanoparticulate Suspension Containing
HPMC, SLS and Simethicone
[0372]The purpose of this study was to prepare a nanoparticulate
suspension of a structurally different water insoluble compound capable
of forming a cyclodextrin inclusion complex (Phenyloin,
5,5-diphenylhydantoin) to further exemplify the benefits of stabilizing
nanoparticulate compositions with a complexing agent.
A milling slurry (164 g) containing by weight percent 20 wt % Phenyloin 5%
wt HPMC, 0.1 wt % SLS, 0.03 wt % simethicone 30% emulsion and 74.87%
deionized water was milled in the same manner as described in Example 7
for 35 minutes using 0.3 mm zirconium oxide balls (260 ml, 85% of chamber
volume). The particle size (D50) after milling was 0.150 .mu.m
unsonicated/0.127 .mu.m after 1 min sonication.
Examples 9A-B
Preparing Phenytoin Nanoparticulate Compositions with and without a
Complexing Agent
[0373]The purpose of this example was to create complexed and uncomplexed
phenyloin nanoparticulate suspensions to further exemplify the benefits
of a complexing agent and an ionic dispersion modulator in forming more
stable solid nanoparticulate compositions.
Example 9A
Uncomplexed Phenyloin Nanoparticulate Compositions
[0374]A milling slurry (1500 g) comprising a mixture of 20% wt phenyloin,
5 wt % HPMC (Pharmacoat 603), 0.1 wt % SLS and 0.028 wt % simethicone 30%
emulsion was milled in a DYNO Mill KDL as described in Example 6 for a
residence time of 26 minutes (total milling time of 145 minutes) to
obtain 1419.6 g of milled suspension after filtration. The D50 after
milling was 0.141 .mu.m unsonicated and 0.128 .mu.m after 1 minute
sonication. The uncomplexed composition after 5 days at room temperature
had a D50 of 0.169 .mu.m unsonicated/0.144 .mu.m after 1 minute
sonication.
Example 9B
Complexed Phenytoin Nanoparticulate Compositions
[0375]To a portion of the milled phenyloin suspension (496.1 g) of Example
9A was added methyl anthranilate (2 g, 0.4%) as a complexing agent. The
milled material with the complexing agent was allowed to cure for 5 days.
The D50 for the complexed material after 5 days of curing time was 0.206
.mu.m unsonicated/177 .mu.m after 1 minute sonication.
[0376]The complexed and uncomplexed suspensions were used to create solid
dose nanoparticulate phenyloin compositions described in Examples 18 and
24.
Example 10
Stability Studies of Complexed and Uncomplexed Aqueous Phenyloin
Nanoparticulate Compositions in SGF and SIF
[0377]This example demonstrates that enhanced stability of a phenyloin
nanoparticulate suspension in USP simulated gastric and intestinal fluids
can be obtained by addition of a complexing agent.
[0378]A sample of the uncomplexed phenyloin nanoparticle suspension (17 g)
prepared in Example 8 was added methyl anthranilate (71.4 mg, 0.42%) and
the suspension was allowed to cure for 5 days at room temperature
(25.degree. C.).
[0379]The initial D50 value for the uncomplexed suspensions at the time of
study were 0.162 .mu.m unsonicated/0.123 .mu.m after 1 minute sonication,
whereas the initial D50 value for the complexed suspensions were 0.169
.mu.m unsonicated/0.159 .mu.m after 1 min sonication.
[0380]The uncomplexed and complexed suspensions were incubated side by
side in SGF and SIF using the method described in Example 3. The
uncomplexed composition visibly flocculated and settled to the bottom of
the vials after 1 hour whereas the complexed composition remained
dispersed in both conditions for the 3 hour period. Additionally, the
complexed composition in both SGF and SIF showed less particle size
changes when examining both unsonicated and sonicated D50 values to
initial values as well as demonstrating less loose aggregation
(difference between D50 unsonicated and sonicated for 1 minute). The
results are shown in Table 1.
TABLE-US-00002
TABLE 1
D50 values for Complexed and Uncomplexed Aqueous
Phenytoin Nanoparticulate Compositions Before
and After Incubation in SGF and SIF
Methyl D50 (.mu.m)
anthranilate Initial D50 (.mu.m) unsonicated/1 min
(% wt/ unsonicated/1 min sonication after 3 Incubation
Entry Phenytoin) sonication hours incubation Medium
1 2.1 0.169/0.159 0.302/0.219 SGF
2 2.1 0.169/0.159 0.316/0.211 SIF
3 0 0.162/0.123 0.868/0.322 SGF
4 0 0.162/0.123 1.18/0.298 SIF
Examples 11A-C
Comparative Stability Studies of Complexed and Uncomplexed Ganaxolone
Nanoparticle Suspensions
[0381]This example demonstrates the enhanced stability of ganaxolone
nanoparticulates complexed with methylparaben compared with uncomplexed
ganaxolone nanoparticulates after incubation in SGF, SIF, heating to
100.degree. C. and conducting several freeze/thaw cycles.
Example 11A
Stability in SGF and SIF at 36-38.degree. C.
[0382]The complexed ganaxolone nanosuspension of Example 4 and uncomplexed
ganaxolone nanosuspension of Example 5A after a curing time (for
complexed preparations) of at least 7 days of storage at room temperature
(20-25.degree. C.) were incubated side by side in SGF and SIF using the
method described in Example 3. The D50 of the complexed formulation
(Entry 1, Table 2) increased only slightly (<23% unsonicated and 9%
after 1 minute sonication) from its initial values. In contrast, the D50
of the uncomplexed formulation (Entry 2, Table 2) increased at least 560%
unsonicated and 153% after 1 minute sonication from its initial values.
The 1.5-fold increase in D50 after sonication indicates the formation of
either strong aggregation or particle growth. Similar trends were
observed after doubling the amount of HPMC and SLS versus ganaxolone
(Entries 3-4, table 2). Doubling the HPMC and SLS amounts versus
ganaxolone was achieved by diluting a 5 g sample from Examples 4 and 5
with 5 g of deionized water containing 5 wt % HPMC, 0.3 wt % SLS and
0.033 wt % simethicone (30% emulsion).
TABLE-US-00003
TABLE 2
Comparative gastric and intestinal stability studies of methylparaben
complexed (initial D50: 0.320 .mu.m unsonicated/0.309 .mu.m after 1 minute
sonication) and uncomplexed (initial D50: 0.136 .mu.m unsonicated/0.112
.mu.m 1 minute sonication) ganaxolone nanoparticle suspensions
D50 (.mu.m)
HPMC SLS Methylparaben No Sonication/1 Test
Entry %(wt/GNX) %(wt/GNX) %(wt/GNX) min sonication conditions.sup.1
1 24.4 1.46 0.98 0.382/0.324 A
0.394/0.326 B
2 23.5 1.41 0 0.897/0.290 A
7.36/0.283 B
3 47.1 2.82 0 0.828/0.258 A
0.933/0.267 B
4 48.8 2.93 0.98 0.350/0.314 A
0.353/0.313 B
.sup.1Incubation conditions: A, SGF, 36-38.degree. C., 3 h; B. SIF,
36-38.degree. C., 3 h see Example 3 for method.
Example 11B
D50 Stability of Complexed and Uncomplexed Ganaxolone Liquid
Nanoparticulate Compositions After Heating at 100.degree. C.
[0383]The milled compositions of Example 4 (complexed) and Example 5A
(uncomplexed) (approximately 2 g each) were placed in 25 mL glass vials
and sealed with a plastic cap. The vials were heated in a 100.degree. C.
oil bath. The D50 of the complexed formulation did not change after
heating for 4 h (both unsonicated and 1 minute sonication) (Table 3). In
contrast, D50 of the uncomplexed suspension continued to grow over the 4
hour period and doubled in size from initial values as shown in Table 3.
TABLE-US-00004
TABLE 3
Changes in D50 values for Complexed and Uncomplexed
Liquid Ganaxolone Nanoparticulate Compositions
D50 (.mu.m) after 20 D50 (.mu.m) after
Initial D50 (.mu.m) min at 100.degree. C. 4 h at 100.degree. C.
Suspension unsonicated/after unsonicated/after unsonicated/after
Formulation 1 min sonication 1 min sonication 1 min sonication
Methylparaben 0.320/0.298 0.326/0.311 0.320/0.310
complexed
Uncomplexed 0.149/0.140 0.246/0.207 0.317/0.302
Example 11C
Stability of Complexed and Uncomplexed Ganaxolone Compositions After
Freeze/Thaw Cycles
[0384]Ganaxolone formulations of Example 4 (complexed) and Example 5A
(uncomplexed) were tested for freeze thaw stability as follows:
[0385]Ten grams of each formulation was placed into a 25 ml HDPE
scintillation vial with HDPE cap. These were placed into a 500 ml glass
beaker containing approx. 1 inch of Styrofoam packing (to slow freezing
process) and placed into an insulated carton containing crushed dry ice.
The vials were stored overnight and then thawed at room temperature for 1
hour. This process was repeated until 3 freeze/thaw cycles had been
completed. The D50 was measured and compared to control material stored
at room temperature in the same container closure system. The D50 of the
complexed formulation did not change after 3 freeze/thaw cycles (Table
4). In contrast, D50 of the uncomplexed formulation increased 450%
(unsonicated) and 144% (1 minute sonication) after the same treatment
(Table 4).
TABLE-US-00005
TABLE 4
Particle size (D50) before and after freezing/thaw cycles for complexed
ganaxolone particles and uncomplexed ganaxolone particles
Initial D50 (.mu.m) D50 (.mu.m) after 3 freeze/
unsonicated/after thaw cycles unsonicated/
Formulation 1 min sonication after 1 min sonication
Methylparaben 0.320/0.298 0.319/0.310
complexed
Uncomplexed 0.149/0.140 0.822/0.341
Example 12
Stability of Complexed Ganaxolone Aqueous Nanoparticulate Suspensions in
SGF and SIF
[0386]Aliquots of the uncomplexed ganaxolone suspension from Example 6
were diluted with either diluent A or diluent B (diluent composition
listed in tabular form below) in 1:2 ratio (Example 6 Suspension/Diluent)
to provide two 75 mg/ml ganaxolone nanoparticle suspension; One with 0.1
wt % methylparaben and 0.02 wt % propylparaben as complexing agents
(Diluent A) and the other with 0.09 wt % sodium benzoate as the
complexing agent with pH adjusted to 4 by the sodium citrate buffer
(Diluent B). Additionally both formulations contained the following: 5 wt
% HPMC, 1 wt % PVA, 0.1 wt % SLS. The two formulations were allowed to
cure for at least 5-7 days (paraben complexed formulation) and 20 days
(sodium benzoate complexed formulation) to reach a stable particle size
(D50) of 0.314 .mu.m (unsonicated)/0.311 .mu.m (after 1 minute
sonication) for the paraben complexed formulation and 0.321 .mu.m
(unsonicated)/0.314 .mu.m (after 1 minute sonication) for the sodium
benzoate complexed formulation at a pH of 4.
TABLE-US-00006
Diluent A Diluent B
Ingredients % wt % wt
Hypromellose (Pharmacoat 603) 5.00 5.00
Polyvinyl Alcohol 1.50 1.50
Sodium Lauryl Sulfate 0.10 0.10
Methylparaben 0.15 0.00
Propylparaben 0.03 0.00
sodium benzoate 0.00 0.14
citric acid anhydrous 0.00 0.18
Sodium citrate 0.00 0.014
Deionized water 93.22 93.07
Total: 100.00 100.00
[0387]The complexed ganaxolone nanoparticulate suspensions as described
above were incubated in SGF and SIF at 36-38.degree. C. for 3 h as in the
method described in Example 3. The results are listed in Table 5 which
showed virtually no increase in particle size (D50) after incubation in
SGF and SIF.
TABLE-US-00007
TABLE 5
Test results in SGF and SIF for Complexed and Uncomplexed
Aqueous Nanoparticulate Ganaxolone Compositions
D50 (.mu.m) after D50 (.mu.m) after
Complexing incubation in SGF incubation in SIF
agent/amount Initial D50 (.mu.m), for 3 h, no for 3 h no
(% wt of total unsonicated/after sonication/after sonication/after
Entry formulation) 1 min sonication 1 min sonication 1 min sonication
A Methylparaben/0.1% 0.314/0.311 0.326/0.313 0.344/0.330
Propylparaben/0.02%
B Sodium 0.321/0.314 0.322/0.312 0.329/0.313
benzoate/0.09%
Citric acid/0.12%
Sodium
citrate/0.0093%
.sup.a The composition of the test formulations are: 7.5 wt % ganaxolone,
5 wt % HPMC, 1 wt % PVA, 0.1 wt % SLS in addition to the amounts of
complexing agents and pH adjusting agents listed in Table 5.
Example 13
SGF Stability of Methyl Anthranilate Complexed Versus Uncomplexed
Ganaxolone Nanoparticulate Suspensions
[0388]To the uncomplexed ganaxolone nanoparticulate suspension prepared as
in Example 6 was added 0.1 wt % or 0.4 wt % methyl anthranilate. All
suspensions (with and without methyl anthranilate as the complexing
agent) were kept at room temperature to allow sufficient curing time to
obtain complexed particles. The complexed suspensions were tested in SGF
with the uncomplexed control as per Example 3. The results are shown in
Table 6 below. The complexed formulation showed virtually no change from
initial after incubation in SGF. In contrast, the uncomplexed control
showed 3-fold increase in D50 unsonicated and 1.6-fold after 1 min
sonication.
TABLE-US-00008
TABLE 6
D50 values for Complexed (methyl anthranilate) and Uncomplexed
Aqueous Ganaxolone Nanoparticulate Compositions in SGF
Initial D50 (.mu.m) D50 (.mu.m) in SGF
Formulation unsonicated/after unsonicated/after
Type 1 min sonication 1 min sonication
Uncomplexed 0.215/0.188 0.656/0.312
Complexed with 0.1 wt % 0.311/0.306 0.363/0.306
Methyl Anthranilate
Complexed with 0.4 wt % 0.480/0.460 0.541/0.465
Methyl Anthranilate
Example 14
Preparation of Pharmaceutically Useful Complexed Ganaxolone Suspension
Formulations (50 mg/mL) from Milled Uncomplexed Ganaxolone
Nanoparticulate Suspensions
[0389]This example illustrates the dilution to 50 mg/mL ganaxolone
nanoparticulate suspension formulations.
Method A (One-Step Dilution):
[0390]An uncomplexed ganaxolone nanoparticulate suspension of known
ganaxolone concentration prepared as described in Example 5A is diluted
with appropriate amount of diluent containing appropriate levels of
excipients and other necessary components such as preservatives,
complexing agents, flavoring, sweetener and antifoaming agent to achieve
50 mg/mL drug concentration.
Method B (Two-Step Dilution):
[0391]An uncomplexed ganaxolone nanoparticulate suspension prepared as
described in Example 5A is first diluted to an intermediate drug
concentration (ca. 80 mg/mL) with appropriate amount of diluent
containing appropriate levels of surface stabilizers excipients and all
necessary components such as preservatives, complexing agents,
antifoaming agents, flavoring and sweeteners. For example, for a milled
uncomplexed ganaxolone nanoparticulate suspension with an initial
(milling slurry) ganaxolone concentration of 25 wt % is diluted by mixing
one part of the milled suspension with two parts of the diluent to obtain
an intermediate concentration of complexed ganaxolone nanoparticulate
suspension of about 8 wt %. The precise ganaxolone concentration is then
determined by appropriate assay (e.g. HPLC). The final dilution to 50
mg/mL ganaxolone is performed with an appropriate amount of diluent
containing the correct levels of all excipients and other components.
Example 15
Preparation of Solid Nanoparticulate Particles Via Rotary Evaporator
Drying and Composition Optimization for Solid Nanoparticulate
Compositions
[0392]This method was applied for ganaxolone nanoparticulate composition
optimization. The method described below can be generally applied to
other water insoluble nanoparticulate compositions.
General Method for Drying Aqueous Nanoparticulate Compositions to Solids
[0393]A general method for drying small samples of complexed and
uncomplexed nanoparticulate compositions for solid dose optimization
studies is as follows: One gram of complexed or uncomplexed
nanoparticulate suspension was placed in a 25 ml glass scintillation vial
then fitted onto a Buchi rotary evaporator R-124. The vial was rotated at
150-175 rpm and the water bath temperature set at 70.degree.-90.degree.
C. Full vacuum was applied (2 to 4 mbar) over a 2 minute period and
continued for 20 to 25 minutes until all visible signs of moisture were
gone. This method yields vials containing solids which are used for
incubation studies.
[0394]During optimization for a solid composition, additional components
were added to the nanoparticulate suspensions prior to drying as follows:
The components were weighed into the vial first and 0.5 g of deionized
water was added to dissolve or disperse the component(s). To this
solution/suspension was added 1.0 g of the nanoparticulate suspension.
The contents of the vial were swirled manually for 15-30 seconds followed
by evaporation of water as described above.
Example 16
Stability of Complexed and Uncomplexed Solid Ganaxolone Nanoparticulate
Compositions in SGF and SIF
[0395]Complexed and uncomplexed aqueous ganaxolone milled suspensions from
Examples 4 and 5A respectively were used and additional components were
added and removal of water was conducted as by the method described in
Example 15.
[0396]D50 changes from the initial values with and without sonication are
listed in Table 7. Incubation in SGF and SIF were conducted using the
method described in Example 3. Complexed Ganaxolone nanoparticles showed
2-4 fold increase in unsonicated D50 values versus initial values. No
change in sonicated D50 values was observed. Uncomplexed ganaxolone
nanoparticles showed a 27-fold increase in unsonicated D50 values versus
initial values and still showed a 7-9-fold increase in sonicated D50
values versus initial values. For the complexed formulation, addition of
sucrose prior to drying reduced aggregation and/or particle size growth
(2-fold increase in D50 unsonicated in SIF versus initial and no increase
in D50 values sonicated or unsonicated in SGF from initial). In contrast,
the uncomplexed formulation with sucrose added still showed unsonicated
D50 increasing >18-fold versus initial values, and at least a doubling
of the D50 from initial values with sonication.
TABLE-US-00009
TABLE 7
Comparative Incubation Results in SGF and SIF of Dried Ganaxolone
Nanoparticulate
Compositions: Methylparaben Complexed (Initial D50: 0.310 .mu.m
unsonicated/0.298
.mu.m after 1 minute sonication) versus Uncomplexed (Initial D50: 0.147
.mu.m
unsonicated/0.140 .mu.m after 1 minute sonication).
D50 (.mu.m)
Sucrose % HPMC SLS % Methylparaben No sonication/1 dispersing
Entry (wt/GNX) (wt/GNX) (wt/GNX) % (wt/GNX) min sonication
conditions.sup.1
1 0 47.1 2.82 0 4.02/1.12 SGF, 3 h
4.13/1.24 SIF, 3 h
2 0 48.8 2.93 0.98 0.636/0.314 SGF, 3 h
1.28/0.322 SIF, 3 h
3 103.8 46.7 2.8 0.98 0.383/0.292 SGF, 3 h
0.588/0.304 SIF, 3 h
4 104.4 47.1 3.1 0 2.72/0.293 SGF, 3 h
5.46/0.301 SIF, 3 h
.sup.1All conditions run as in Example 3
Examples 17A-B
Effect of an Ionic Dispersion Modulator in Complexed and Uncomplexed
Ganaxolone Nanoparticulate Solid Compositions
[0397]This example shows the effect of various amounts of an ionic
dispersion modulator (e.g., sodium chloride) on stabilizing and reducing
the amount of sucrose needed to reduce changes in D50 values (from
initial) when dispersed in SGF and SIF.
Example 17A
Preparation of Solid Ganaxolone Nanoparticulate Compositions Containing an
Ionic Dispersion Modulator by Rotary Evaporator Drying
[0398]The following is an example of preparing solid complexed and
uncomplexed ganaxolone nanoparticulate compositions listed in Table 8 by
the method of Example 15. Other compositions listed in Table 8 were
prepared using the same procedure by adding the appropriate amount of
salt and sucrose unless otherwise specified in Table 8.
[0399]The following components were placed in a 25 ml glass scintillation
vial: 5.13 mg of sucrose crystals and 12.5 mg of 25 wt % sodium chloride
solution. Deionized water (0.5 g) was then added to dissolve the sucrose
crystals and to achieve a homogeneous solution.
[0400]The complexed ganaxolone suspension (1 g) of Example 4 containing
20.5 wt % ganaxolone, 5.0 wt % HPMC, 0.3 wt % sodium lauryl sulfate, 0.2
wt % methylparaben 0.03 wt % simethicone (30% emulsion in water) was then
added to the vial and the mixture was swirled to mix well. The contents
in the vial were then dried per Example 15. This produced the composition
listed in Table 8, Entry 7.
TABLE-US-00010
TABLE 8
Compositions Demonstrating benefits
of an Ionic Dispersion modulator
Nanoparticulate NaCl Deionized
Ganaxolone solution water
Entry .sup.c Suspension (g) (25 wt %) Sucrose (g) (g)
1 1.0 0.3 0 0.5
2 1.0 0.1 0 0.5
3 1.0 0.050 0 0.5
4 1.0 0.025 0 0.5
5 1.0 0.0125 0 0.5
6 1.0 0.0125 0.01025 0.5
7 1.0 0.0125 0.00513 0.5
8 1.0 0.0164 0 0.5
9 1.0 .sup. 0.050 .sup.a 0 0.5
10 1.0 0 0 0.5
.sup. 11 .sup.b 1.0 .sup. 0.050 .sup.a 0 0.5
.sup.a Salt was added as solid;
.sup.b The nanoparticle slurry was from Example 5A;
.sup.c Complexed Ganaxolone suspension from Example 4 was used in Entry
Nos. 1-10.
Example 17B
Dispersion Results of Dried Complexed and Uncomplexed Ganaxolone
Nanoparticles in Both SGF and SIF
[0401]Table 9 shows the degree of aggregation of solid nanoparticulate
complexed and uncomplexed ganaxolone compositions incubated in SGF and
SIF. The Entry number in Table 9 corresponds to the compositions given in
Table 8.
[0402]Sodium chloride as an ionic dispersion modulator is very effective
in preventing aggregation in SGF and SIF when used with a complexed
nanoparticle formulation. Addition of an ionic dispersion modulator also
allows the complexed solid nanoparticulate formulation to have a higher
drug concentration by requiring less of a water soluble spacer (e.g.
sucrose) to achieve minimal aggregation. This ability to create more
stable and concentrated solid formulation is needed in preparing
commercially viable compositions of drugs requiring a high dose.
[0403]Addition of an ionic dispersion modulator allows for more
concentrated drug compositions.
TABLE-US-00011
TABLE 9
Effect of an Ionic Dispersion Modulator on the Dispersion of Dried
Ganaxolone Compositions (With
and Without a Complexing Agent) in Simulated Gastric and Intestinal Fluid
(SGF and SIF)
Simethicone Methyl- D50(.mu.m)
HPMC SLS 30% emulsion paraben NaCl Sucrose unsonicated/1 Dispersion
Entry % wt/GNX % wt/GNX % wt/GNX % wt/GNX % wt/GNX % wt/GNX min sonication
conditions.sup.1
10 24.4 1.46 0.15 0.98 0 0 13.2/0.332 A
0.286 B
9 24.4 1.46 0.15 0.98 24.4 0 0.344/0.319 A
11 23.5 1.41 0.14 0 23.5 0 22.7/8.9 A
5 24.4 1.46 0.15 0.98 1.5 0 3.17/0.337 A
4.45/0.353 C
6 24.4 1.46 0.15 0.98 1.5 5 0.364/0.316 A
0.396/0.322 C
0.490/0.331 D
0.561/0.329 E
7 24.4 1.46 0.15 0.98 1.5 2.5 0.395/0.323 A
0.370/0.312 C
0.416/0.326 D
0.533/0.331 E
8 24.4 1.46 0.15 0.98 2.0 0 0.548/0.334 A
0.506/0.326 C
4 24.4 1.46 0.15 0.98 3.0 0 0.355/0.319 A
0.367/0.315 C
0.485/0.329 D
0.609/0.334 E
3 24.4 1.46 0.15 0.98 6.1 0 0.338/0.314 A
0.429/0.337 C
2 24.4 1.46 0.15 0.98 12.2 0 0.353/0.317 A
0.367/0.318 C
9 24.4 1.46 0.15 0.98 24.4 0 0.440/0.322 D
0.459/0.324 E
1 24.4 1.46 0.15 0.98 36.6 0 0.346/0.315 A
0.372/0.317 C
.sup.1Dispersion conditions: A, SGF, 5 min, rt; B, deionized water, 5 min,
rt; C, SIF, 5 min, rt; D, SGF, 3 h, 36-38.degree. C., stirred; E, SIF, 3
h, 36-38.degree. C., stirred.
Example 18
Effect of an Ionic Dispersion Modulator (Sodium Chloride) on Complexed and
Uncomplexed Nanoparticulate Phenyloin Solid Compositions
[0404]The complexed and uncomplexed phenyloin nanoparticulate suspensions
of Example 9, were diluted (1:1 by weight, 5 g of each) with deionized
water containing 6.25 wt % HPMC and 0.125 wt % SLS to obtain phenyloin
nanoparticulate suspensions containing 10 wt % phenyloin, 5.625 wt %
HPMC, 0.1125 wt % SLS for rotary evaporated drying. The suspensions (0.5
g) containing appropriate amount of urea and/or sodium chloride were
dried on a Buchi rotary evaporator using the method described in Example
15 to obtain dried phenyloin nanoparticulate powders. The dried phenyloin
nanoparticulate powders were incubated in SGF per Example 3. The results
are shown in Table 10 below:
TABLE-US-00012
TABLE 10
Effect of an Ionic Dispersion Modulator (NaCl) on the Dispersion
of Rotary Evaporated Solid Complexed and Uncomplexed Phenytoin
Nanoparticulate Compositions in SGF.
D50 (.mu.m) after
incubation in SGF
HPMC SLS Methyl Sucrose Urea NaCl (36.degree.-38.degree. C., 70 minutes)
% wt/ % wt/ anthranilate % wt/ % wt/ % wt/ 1 min
Entry API API % wt/API API API API Unsonicated sonication
1.sup.a 56.25 1.125 2 0 0 0 5.87 0.299
2.sup.a 56.25 1.125 2 0 100 0 3.493 0.273
3.sup.a 56.25 1.125 2 0 0 5 8.914 0.353
4.sup.a 56.25 1.125 2 10 0 5 23.64 5.961
5.sup.a 56.25 1.125 2 0 8 5 0.405 0.249
0.283 0.206
(DI water) (DI water)
6.sup.a 56.25 1.125 2 0 8 0 3.894 0.287
0.290 0.216
(DI water) (DI water)
7.sup.a 56.25 1.125 2 0 0 20 0.325 0.228
8.sup.b 56.25 1.125 0 0 8 5 16.642 1.926
.sup.aPrepared from methyl anthranilate (0.4 wt %) complexed phenytoin
nanoparticulate suspension with initial D50 (.mu.m) of
0.211(unsonicated)/0.187(after 1 min sonication);
.sup.bPrepared from uncomplexed phenytoin nanoparticulate suspension with
initial D50 (.mu.m) of 0.161(unsonicated)/0.141 (after 1 min sonication).
In the above example, urea was identified as a water soluble spacer.
Examples 19-20
[0405]Examples 19-20 below demonstrate that certain complexed ganaxolone
spray dried and spray layered compositions containing an ionic dispersion
modulator have less aggregation in SGF and SIF (unsonicated) by a factor
of greater than 10-fold. Additionally the examples below show less
aggregation for certain complexed phenyloin nanoparticulate formulations
than for uncomplexed.
Example 19
Preparation of Complexed Ganaxolone Nanoparticulate Suspension for Spray
Layering and Spray Drying
[0406]Complexed ganaxolone nanoparticulate suspensions for spray layering
and spray drying were prepared by milling a slurry (7000 g) containing
28.3 wt % ganaxolone, 3 wt % HPMC, 0.15 wt % SLS and 0.033 wt %
simethicone (as a 30% emulsion) as described in Example 6. After milling,
a complexing agent (methylparaben sodium, 12.60 g), SLS (11.52 g), citric
acid anhydrous (13.91 g) and deionized water (3972.93 g) were added and
stirred for 20 minutes. After stirring, the suspension was packaged in a
HDPE container and kept at room temperature (25.degree. C.) to cure.
After a curing time of 2 weeks, additional components (e.g. sucrose, PEG,
salt) were added and diluted with water to desired concentration for
spray layering or spray drying. D50 values were 0.336 .mu.m
(unsonicated)/0.332 .mu.m (after 1 min sonication).
Examples 20A-C
Spray Layered Complexed and Uncomplexed Ganaxolone Nanoparticulate
Composition
[0407]The spray-layered complexed and uncomplexed ganaxolone
nanoparticulate compositions of Examples 20A-C were prepared using the
following method:
[0408]A Mini Glatt 8560 (Glatt Air Techniques, Ramsey, N.J.) was
configured for fluid bed coating using a 0.5 mm Schlick nozzle with a
Wurster column (3.5 cm.times.9.5 cm) set 10 mm above the bottom of the
chamber floor. The temperature of the bed was monitored with an internal
probe. A peristaltic pump was used to introduce the spray solutions
through the nozzle. The unit was first pre-heated for one hour at
56.degree. C. The bed chamber was opened and 40 g of MCC beads (Celphere,
CP-305) was introduced and a pressure of 0.36 bar was used to fluidize
the bed. To minimize electrostatic charges, water was immediately sprayed
(atomization pressure 0.26 bar). After 1-2 minutes of spraying, the feed
line was switched to a stirred vessel containing the ganaxolone spray
slurry.
[0409]Examples 20A and 20B demonstrate optimization of SGF dispersion
testing results of a complexed ganaxolone spray layered composition
(immediate release) for dog pharmacokinetics described below in Example
27. Example 20C describes spray layering of an uncomplexed ganaxolone
nanoparticulate composition.
[0410]The ingredients contained in the solid composition of each of the
compositions of Examples A-C are shown in Table 11A.
TABLE-US-00013
TABLE 11A
Solid composition of spray layered ganaxolone nanoparticulate
compositions (complexed vs uncomplexed)
Solid Composition (% wt of total solid excluding MCC cores)
Methyl
Spray PEG PEG Sodium paraben Citric Methyl Simethi-
Form GNX HPMC SLS 400 4000 Sucrose chloride sodium acid paraben cone
20A 69.54 20.05 2.37 3.92 0 0 3.13 0.46 0.50 0 0.02
20B 49.99 12.30 0.26 0 3.16 33.36 0.64 0 0 0.28 0.02
20C 68.16 16.04 0.96 0 14.81 0 0 0 0 0 0.03
[0411]The dispersion testing results for each of the compositions of
Examples 20A-C are shown in Table 11B.
TABLE-US-00014
TABLE 11B
Dispersion Results in SGF or Water
Initial D50 Dispersion D50
(.mu.m) (.mu.m)
Spray unsonicated/1 unsonicated/1 Testing
Formulation min sonication min sonication Conditions.sup.A
20A 0.339/0.332 6.67/0.369 SGF,
20B 0.356/0.346 0.395/0.370 SGF,
0.366/0.343 Deionized Water
20C 0.170/0.160 0.202/0.196 Deionized Water
5.57/0.392 SGF,
.sup.AConditions were 36-38.degree. C. for 3 hours unless specified
otherwise.
Example 20A
Complexed Ganaxolone Spray Formulation
[0412]A total of 38.1 g of the ganaxolone spray slurry was sprayed over 39
minutes (average spray rate approximately 1 ml/min). The bed temperature
ranged from 45 to 49.degree. C. The spray layered beads were dried for an
additional 7 minutes after the spraying was completed. Spray layered
beads (47 g) were isolated. Theoretical loading of layered solid: 19.7%.
Example 20B
Complexed Ganaxolone Spray Formulation
[0413]A total of 80 g of slurry was sprayed onto 40 g of MCC beads
(Celphere CP-305) over a period of 105 minutes to obtain 63 g of spray
layered beads (57.5% loading). The bed temperature was maintained at
43-47.degree. C. and inlet air temperature was 54.degree. C.
Example 20C
Uncomplexed Ganaxolone Spray Formulation
[0414]This spray formulation was prepared by adding PEG 4000 (3 wt % of
total formulation) to the uncomplexed ganaxolone nanoparticulate
suspension of Example 5A. A total of 93 g of slurry was sprayed onto 40 g
of MCC beads (Celphere CP-305) over a period of 110 minutes to obtain 58
g of spray layered beads (45% loading). The bed temperature was
maintained at 36-44.degree. C. and inlet air temperature was 48.degree.
C.
Examples 21A-B
Spray Dried Complexed and Uncomplexed Ganaxolone Nanoparticulate
Composition
Example 21A
Spray Dried Complexed Ganaxolone Nanoparticulate Compositions
[0415]To the complexed ganaxolone nanoparticle suspension of Example 19
was added sucrose, and sodium chloride. The mixture was diluted with
deionized water to obtain the following composition suitable for spray
drying: 14.47 wt % Ganaxolone, 1.91 wt % HPMC, 0.96 wt % SLS, 2.15 wt %
sucrose, 1.43 wt % NaCl, 0.04 wt % methylparaben and 0.006 wt %
simethicone 30% emulsion. This slurry (478 g) was spray dried on a Buchi
B-191 Mini Spray Drier to obtain 63.4 g of dry ganaxolone nanoparticle
powder. The process parameters were as the following: average spray rate:
5.3 g/min; outlet temperature: 64-66.degree. C.; inlet temperature:
108-114.degree. C.; airflow: 85% aspiration. D50 values for the
ganaxolone nanoparticles were 0.329 .mu.m unsonicated/0.318 .mu.m after 1
minute sonication upon re-dispersion in water. D50 values in SGF were
0.317 .mu.m unsonicated/0.306 .mu.m 1 minute sonication.
Example 21B
Spray Dried Uncomplexed Ganaxolone Nanoparticulate Composition
[0416]To an uncomplexed ganaxolone nanoparticle suspension milled in a
similar fashion as described in Example 6 was added PEG 3350 and diluted
with deionized water to obtain the following composition: 22.88 wt %
Ganaxolone, 4.78 wt % HPMC, 0.19 wt % SLS, 4.31 wt % PEG 3350 and 0.032
wt % simethicone 30% emulsion. This slurry was spray dried on a Buchi
B-191 Mini Spray Drier in a similar fashion as described in above Example
20A to obtain dry ganaxolone nanoparticulate powder in 62% yield. D50 of
the ganaxolone nanoparticles was 0.249 .mu.m unsonicated/0.220 .mu.m
after 1 minute sonication upon re-dispersion in water. D50 in SGF was
4.71 .mu.m unsonicated/2.54 .mu.m after 1 minute sonication.
Example 22
Preparation of an Enteric Coated (Controlled Release) Complexed Ganaxolone
Formulation
[0417]The complexed spray layered beads prepared as described in Example
20B is spray coated with an enteric coating formulation having the
following composition:
TABLE-US-00015
Component Amount (g)
Eudragit L30 D-55 (Degussa) 96
Triethyl citrate 4
Talc 8
Water 95
[0418]The coating process is carried out as follows:
[0419]Charge 140 g of spray layered IR beads and 1 g talc to the
pre-heated mini Glatt, which has been configured with a 3.5 cm.times.9.5
cm Wurster column and a 0.5 mm Schlick nozzle as described in Examples
20A-C. The thermostat on the Glatt is set to 40.degree. C. and the drying
air pressure to 0.20 bar.
[0420]Eudragit enteric coating formulation is introduced to the mini Glatt
via a peristaltic pump that is positioned in close proximity. The coating
formulation is well stirred during the coating. The Eudragit slurry is
added at 2.5 ml/min with an atomization pressure of 0.92 bar. The bed
temperature is maintained between 26 and 28.degree. C.
[0421]After completion of the coating process, the coated beads are
allowed to cool for 5 minutes. After cooling, one hundred and thirty
grams (130 g) of the Eudragit slurry is coated onto the beads. This
amounts to 18.4% of coating solids. The weight of the coated beads
isolated is 166 g.
Example 23
Preparation of Solid Complexed Ganaxolone Particles Via Spray Granulation
[0422]A Mini Glatt (Glatt Air Techniques, Ramsey, N.J.) is configured for
top spray with a fluid bed. A 0.5 mm Schlick-type nozzle is inserted
above the fluid bed. Then, 50 g of lactose monohydrate (Kerry) is added
and fluidized with 0.27 bar pressure. The apparatus is heated to
50.degree. C. for approximately 30 min with bed fluidization pressure of
0.20-0.25 bar.
[0423]A ganaxolone slurry comprising 14 wt % ganaxolone, 3.5 wt % HPMC, 8
wt % sucrose, 0.08 wt % methylparaben, 0.07 wt % sodium benzoate, 0.14%
citric acid, 0.9 wt % PEG 4000, 0.4 wt % sodium chloride is introduced by
a peristaltic pump through the top-mounted nozzle.
[0424]The spray pressure ranges from 0.27 to 0.35 bar and the bed
temperature is held at 40-45.degree. C. while spraying at 1 to 2 ml/min.
The fine powered lactose becomes granular during the spraying. A total of
36 g of 21% solids is sprayed, for a solids loading of 20%.
Examples 24A-D
A Spray Layered Complexed and Uncomplexed Phenyloin Nanoparticulate
Composition
[0425]A Mini Glatt 8560 was configured for spray layering as described in
Examples 20 A-C. The unit was pre-heated at 60.degree. C. The bed chamber
was opened and 75 g of MCC beads (Celphere, CP-305) was introduced and a
pressure of 0.30-0.32 bar was used to fluidize the bed. To minimize
electrostatic charges, water was immediately sprayed (atomization
pressure 1 bar). After 1-2 minutes of spraying, the feed line was
switched to a stirred vessel containing the phenyloin spray slurry. The
bed temperature was maintained at 36-41.degree. C. during spraying. The
spray layered beads were incubated in SGF per Example 3 and the testing
results are shown in Table 12.
Example 24A
Uncomplexed Phenytoin Spray Composition
[0426]This formulation was prepared by adding sucrose (5.4 g), sodium
chloride (0.2 g), SLS (0.06 g) and deionized water to the uncomplexed
phenyloin nanoparticulate suspension of Example 9 (100.0 g). It was
sprayed at 2.5 ml/min. After completion of the spray layering, 96.8 g of
spray layered beads were obtained. The loading was 29%.
Example 24B
Complexed Phenyloin Spray Composition
[0427]This formulation was prepared and spray layered as described for the
above formulation 24A except using the complexed phenyloin
nanoparticulate of Example 9. After completion of spraying, 101.1 g of
spray layered beads was obtained. The loading was 34.8%.
Example 24C
Uncomplexed Phenytoin Spray Composition
[0428]This formulation was prepared by adding a solution of urea (0.8 g),
sodium chloride (0.5 g) in deionized water (2 g) to the uncomplexed
phenyloin nanoparticulate suspension of Example 9 (50.0 g). The resultant
suspension was diluted with deionized water (50 g) containing 6.25 wt %
HPMC, 0.125 wt % SLS and 0.08 wt % simethicone 30% emulsion. This
suspension was spray layered onto 75 g of the MCC beads (Celphere CP-305)
as described for spray formulation 24A. After completion, phenyloin spray
layered beads (87.2 g) was obtained. The loading of phenyloin on the
beads was 16.2%.
Example 24D
Complexed Phenytoin Spray Composition
[0429]This formulation was prepared and spray layered onto 75 g of MCC
cores as described above for Formulation 24C except using the complexed
phenytion nanoparticulate suspension of Example 9. After completion of
the spray layering, 86.8 g of spray layered beads was obtained. The
loading was 15.7%.
TABLE-US-00016
TABLE 12
Dispersion SGF testing results of spray layered uncomplexed
and complexed phenytoin nanoparticulate compositions.sup.1
D50 (.mu.m) after incubation in
SGF per Example 3 unless
Spray Solid Composition as % weight to Drug specified otherwise
Formu- Methyl 1 min
lation HPMC SLS anthranilate Urea Sucrose NaCl Unsonicated sonication
24A 25.0 0.8 0 0 27.0 1.0 23.34 5.51
24B 25.0 0.8 2 0 27.0 1.0 8.55 0.291
24C 56.25 1.125 0 8 0 5 9.13 0.289
3.74 0.223
(DI water) (DI water)
24D 56.25 1.125 2 8 0 5 0.320 0.267
0.304 0.205
(DI water) (DI water)
.sup.1Initial D50 (.mu.m) values: 0.192 (unsonicated)/0.141 (after 1 min
sonication) for the uncomplexed and 0.209 (unsonicated)/0.177 (after 1
min sonication) for the complexed phenytoin nanoparticulate composition.
[0430]The purpose of the following examples is to describe preparation and
testing of various solid dosage forms comprising drug nanoparticles.
Example 25
Pharmacokinetics of Nanoparticulate Formulations in Beagle Dogs
[0431]Purpose-bred Beagle dogs are obtained and housed in a USDA-approved
facility in accordance with AAALAC guidelines. Expected dog weights are
from 8 to 12.0 kg at the beginning of the evaluation, and are weighed
prior to each period of the study. Animals are block randomized into
groups of 3 per treatment. Each study will test a complexed drug
composition. Fasted animals are fasted overnight with water prior to each
study day. Designated fed dogs are fed a can (about 400 g) of Alpo
"Chunky Beef for Dogs," which has 55% of total calories from fat,
approximately 45 minutes prior to dosing. If the liquid suspension is to
be administered without dilution, the dose is given via oral gavage
followed by a 7.5 to 10 ml/kg water flush. Standard laboratory chow and
water are offered ad libitum 4 h after dosing. To eliminate the
variability of drug absorption among the dogs, all studies should be
conducted in a randomized crossover design. Approximately 2 milliliters
of blood sample are withdrawn with a 21G needle and via direct
venipuncture sampling at predose, 15 min, 30 min, 1 h, 2 h, 4 h, 6 h, 8
h, 10 h, 24 h and 48 h. Blood is immediately transferred to a potassium
EDTA blood collection tube (VACUTAINER, Becton Dickinson, Franklin Lakes,
N.J., USA) and is stored on ice until the samples are centrifuged at
2500-4000 rpm for 15 min. The plasma is transferred to polypropylene
tubes, and samples are stored at -70.degree. C. until analyzed by a
suitable method (e.g. liquid chromatography/tandem weight spectrometry).
Example 26
Dog Pharmacokinetics with Complexed and Uncomplexed Aqueous Ganaxolone
Nanoparticulate Compositions
[0432]The uncomplexed ganaxolone formulation 26A from Example 7 (final
composition of 2.5 wt % ganaxolone, 5 wt % HPMC, 0.1 wt % SLS,) showed an
approx. 3 and 2-fold increase in Cmax and AUC in the Fed and fasted state
respectively. The uncomplexed ganaxolone formulation 26B prepared from a
concentrated slurry as in Example 6 (final composition of 5 wt %
ganaxolone, 5 wt % HPMC, 0.2 wt % SLS and 1 wt % Polyvinyl alcohol (PVA)
(all based on total weight of formulation). Uncomplexed formulation 26B
gave a decrease in Cmax levels and AUC by about 50% as compared to
uncomplexed formulation 26A. Administering the complexed ganaxolone
formulation prepared from a concentrated slurry as in Example 6 (final
composition of 5 wt % ganaxolone, 5 wt % HPMC, 0.1 wt % SLS, 1 wt % PVA,
0.1 wt % methylparaben, 0.02 wt % propyl paraben, 0.09 wt % sodium
benzoate, 0.12 wt % citric acid and 0.0093 wt % sodium citrate) gave the
most desirable pharmacokinetic performance by achieving optimal
bioavailability and reduced variability and Cmax. Achieving a high
bioavailability (AUC) with a larger particle size (2-fold higher due to
complexing agent and curing) was surprising as bioavailability is thought
to increase as the particle size decreases. In the case of Ganaxolone,
complexed compositions of the type in formulation 26C allow for greater
overall exposure while minimizing sedation due to high Cmax values.
TABLE-US-00017
TABLE 13
Comparative PK results in beagle dogs for ganaxolone suspension
formulations at comparable dose levels (5 mg/kg)
PVA/
Complexing
Formulation Particle Size Agent C.sub.max AUC.sub.0-72 hr
Reference (D50) (Methylparaben) (ng/mL) (ng*h/mL) Food Intake
Formulation 26A 110 nm None/None 448 .+-. 96 2422 .+-. 1059 Fasted
Formulation 26A 110 nm None/None 1194 .+-. 104 4637 .+-. 2600 Fed
Formulation 26B 140 nm Yes/None 268 .+-. 36 1643 .+-. 295 Fasted
Formulation 26B 140 nm Yes/None 640 .+-. 92 3525 .+-. 1190 Fed
Formulation 26C 320 nm Yes/Yes 243 .+-. 40 1855 .+-. 321 Fasted
Formulation 26C 320 nm Yes/Yes 642 .+-. 40 5512 .+-. 681 Fed
Example 27
Pharmacokinetic Analysis of Solid Ganaxolone Nanoparticulate Compositions
in Beagle Dogs
[0433]The following example demonstrates that in cases where loose
aggregation can be totally reversed by sonication, a measurable
difference in pharmacokinetic performance can be seen. Although the
impact of loose aggregates on pharmacokinetic performance will be
dependent on specific compounds, this example illustrates with immediate
release complexed ganaxolone spray layered beads in gelatin capsules that
the most preferred embodiments are those that demonstrate the smallest
changes in D50 values measured unsonicated versus after 1 min sonication.
[0434]The solid ganaxolone formulations from Example 20A and 20B were
placed into gelatin capsules to deliver a 5 mg/kg dose of ganaxolone to
beagle dogs in the fasted state. The fasted state was chosen as this
condition tends to show more pharmacokinetic differences in
nanoparticulate formulations of water insoluble drugs. These formulations
were chosen as they were part of the solid dose optimization process and
exhibited different degrees of loose aggregation. As can be seen below in
Table 14, a 3-fold improvement in bioavailability (AUC) was seen with
solid complexed ganaxolone capsules versus capsules containing solid
complexed ganaxolone that demonstrated more loose aggregation in SGF.
TABLE-US-00018
TABLE 14
D50 (.mu.m) in SGF
Formulation Unsonicated/after C.sub.max AUC.sub.0-72 h
Reference 1 min sonication (SD)(ng/mL) (SD)(ng*h/mL)
Formulation 20A 6.67/0.369 150 (94) 756 (332)
Formulation 20B 0.395/0.370 135 (40) 2294 (1574)
SD = Standard Deviation
Example 28
Immediate Release Capsules with and without Complexing Agent
[0435]Suspensions (1200 grams) in water containing 25 wt % ganaxolone, 5.0
wt % hydroxypropyl methylcellulose (Pharmacoat 603), 0.0333 wt % of 30%
simethicone emulsion, and 0.2 wt % sodium lauryl sulfate, either with
0.05 wt % methylparaben (capsule Ex. 1) or with no methylparaben (capsule
Ex. 2, 5.2 wt % of HPMC instead of 5 wt %) are prepared. Each wt % is
based on the total weight of the suspension.
[0436]The ganaxolone particles are milled using conditions as described in
Example 4. For formulations with complexing agent (Capsule Form 1),
ganaxolone nanoparticles having a particle size (D50) of about 120 nm as
measured by Horiba LA 910 particle size analyzer are obtained immediately
after milling. This volume-weighted-median particle size grows to about
220 nm after 7 days of curing at ambient temperature, indicating that
ganaxolone complex is formed. The D50 does not change after this curing
period for the duration of the study. For Capsule Form 2 (without
complexing agent), ganaxolone nanoparticles having the same particle size
(D50) (about 120 nm) are obtained immediately after milling.
[0437]Sucrose (48.5 g) and NaCl (6.5 g) (together about 13 wt % of solids)
and water (800 ml) is added to each of the ganaxolone suspensions for
Capsule Form 1 and 2 and the resulting mixtures are homogenized for 20
minutes for spray drying. The compositions of the mixtures to be spray
dried are given in Table 15.
TABLE-US-00019
TABLE 15
Composition of spray mixture prior to spray layering
Capsule Example 2
Capsule Example 1 Ganaxolone (No Paraben)
Ganaxolone Complex Wt % based on
Weight, Wt %/total Weight, total solid
Component gram solid wt, % gram weight, %
Ganaxolone 300 71.7 300 71.4
HPMC 60 14.3 62.4 14.9
Simethicone 0.12 0.03 0.12 0.03
SLS 2.4 0.57 2.4 0.57
Methylparaben 0.60 0.14 0 0
Sucrose 48.5 11.6 48.5 11.5
Sodium 6.5 1.6 6.5 1.5
chloride
Total 418.12 100 419.92 100
[0438]For each of Capsule Form 1 and 2, 100 grams of microcrystalline
cellulose (MCC) beads (e.g. Celphere, 30/35 mesh) are added to a Glatt
GPCG-3 fluidized bed with Wurster column insert (4 inch), inlet
temperature of about 55.degree. C. and air temp of about 40.degree. C.
(total air volume approx. 175 cubic cm/hr). About 2000 grams of each
spray mixture are sprayed (bottom spray) through 1.2 mm nozzles at 11
ml/min and 1.5 bar of pressure until a layering of about 400 wt % is
achieved as compared to initial beads weight. The theoretical
compositions of the spray layered complexed ganaxolone particles (Capsule
Form 1) and ganaxolone particles (Capsule Form 2) are shown in Table 16.
TABLE-US-00020
TABLE 16
Composition of spray layered beads
Capsule Form 2
Ganaxolone
Capsule Form 1 (No Methyl Paraben)
Ganaxolone Complex Wt % based on
Weight, Wt %/total Weight, total solid
Component gram solid wt, % gram weight, %
Ganaxolone 300 57.9 300 57.7
HPMC 60 11.6 62.4 12.0
Simethicone 0.12 0.02 0.12 0.02
SLS 2.4 0.46 2.4 0.46
Methylparaben 0.60 0.12 0 0
Sucrose 48.5 9.4 48.5 9.3
NaCl 6.5 1.25 6.5 1.25
MCC beads 100 19.3 100 19.2
Total 518.12 100 519.92 100
[0439]The spray layered ganaxolone complexed particles (Capsule Form 1) or
ganaxolone particles (Capsule Form 2) are then filled into gelatin
capsules with a fill weight of 518-520 mg coated beads to achieve a 300
mg dose.
Example 29
Delayed Release Capsules
[0440]Drug complexed particles (e.g., prepared as set forth for the
ganaxolone nanoparticles in the above examples) spray-layered onto inert
beads (500 g) are loaded directly into a rotary granulator/coater (Freund
CF-360 granulator) for enteric coating. The rotating particle bed is
sprayed with a coating solution containing 50 wt % Eudragit.RTM. L
30-D55, 2.5 wt % talc, 1.5 wt % dibutyl sebecate, 20 wt % ethanol, 23.5
wt % isopropyl alcohol, and 2.5 wt % water. A coating level of about 8 wt
% is achieved. The ganaxolone content in each coated bead is about 53.4
wt % based on the total weight of the coated beads.
[0441]A suitable amount of the coated beads are hand-filled into gelatin
capsule shells, respectively, to form modified release capsules. These
particulates are substantially insoluble in the stomach due to the
enteric coating but substantially soluble in the intestine.
Example 30
Coated Tablets
[0442]To spray-dried drug complexed particles (e.g., prepared as set forth
for the ganaxolone nanoparticles in Example 21, Prosolv 90, and
Dipotassium Phosphate Powder are added sequentially into a Bohle Bin
Blender (BL07C, Warminster, Pa., USA) and blended for 10.+-.0.1 minutes
at 11.+-.1 rpm. Additional Prosolv 90 and Sodium Starch Glycolate are
added and blended for 10.+-.0.1 minutes at 11.+-.1 rpm. The material is
then milled and then passed through a 0.5 mm screen (35 Mesh).
TABLE-US-00021
Blend Component Weight % w/w
Silicified Microcrystalline Cellulose, NF 4.255 kg 37.0
(Prosolv 90)
Sodium Starch Glycolate, NF, EP 0.230 kg 2.00
Sodium Chloride 0.287 kg 2.5
Magnesium Stearate 0.0575 kg 0.5
Dipotassium Phosphate Powder, USP, PE 0.230 kg 2.00
Spray dried drug nanoparticle powder 6.44 kg 56.0
Totals 11.5 kg 100.0
[0443]The drug blend is loaded into a tablet compressing machine, such as
a Fette 1200 B Tool Tablet Press (TP06) or equivalent, and tablets are
formed using oval upper and lower punches.
[0444]Optionally, an enteric coat is applied to the tablet cores as
follows: The enteric coating comprising Opadry.RTM. Enteric from
Colorcon.RTM. and the over coat comprising Opadry.RTM. clear applied
sequentially as aqueous coating suspensions using a coating pan. The
tablet cores are preheated to 46.degree. C. (Exhaust air temperature).
The pan speed is adjusted to provide adequate tablet flow and the coating
suspensions are sprayed onto the tablets at an atomizing air pressure of
18-30 psi; an inlet air temperature of 60-70.degree. C. for over coat,
and of 42-50.degree. C. for the enteric coat; an exhaust air temperature
of 40 to 50.degree. C. for the over coat and 30 to 35.degree. C. for the
enteric coat; a spray rate of 15 to 50 ml/min.; and an inlet air flow of
175 to 300 CFM. One of skill in the art will understand that the
processing parameters for coating are dependent in part upon the size of
the batch to be coated and can be adjusted accordingly. The enteric
coating should be applied so that a tablet core weight gain of 8-15 w
%/tablet core weight is achieved. Cellulose acetate phthalate,
hydroxypropyl methylcellulose phthalate, polyvinyl acetate phthalate, a
methacrylic acid copolymer, hydroxypropyl methylcellulose acetate
succinate, shellac, cellulose acetate trimellitate, or a combination
comprising one or more of the foregoing enteric polymers may be used in
place of the Opadry Enteric coating.
[0445]In the preceding specification, the invention has been described
with reference to specific exemplary embodiments and examples thereof. It
will, however, be evident that various modifications and changes may be
made thereto without departing from the broader spirit and scope of the
invention as set forth in the claims that follow. The specification and
drawings are accordingly to be regarded in an illustrative manner rather
than a restrictive sense.
* * * * *