Title of Invention

A PROCESS FOR FORMING A PHARMACEUTICAL COMPOSITION AND A PHARMACEUTICAL COMPOSITION PER SE.

Abstract A PROCESS FOR FORMING A PHARMACEUTICAL COMPOSITION COMPRISING : A) PREPARING CORE PARTICLES COMPRISING AN ACTIVE AGENT OF TOPIRAMATE; B) DRYING THE CORE PARTICLES FROM STEP (A) TO FORM DRIED CORE PARTICLES; HAVING A PARTICLE SIZE OF 0.100 MM TO 2.5 MM; C) COATING THE DRIED CORE PARTICLES FROM STEP (B) WITH A TASTE MASKING MIXTURE TO FORM COATED PARTICLES; AND D) DRYING THE COATED PARTICLES FROM STEP (C) TO FORM THE PHARMACEUTICAL COMPOSITION WHEREIN THE AMOUNT OF TASTE MASKING MIXTURE RANGES FROM 7% BY WEIGHT TO 15% BY WEIGHT OF THE PHARMACEUTICAL COMPOSITION, AND THE COATED PARTICLES HAVE A FINAL PARTICLE SIZE OF 0.100MM TO 2.5MM.
Full Text Trite of the invention.
Pharmaceutical Composition of Topiramate
Cross-Reference to Related Application
This application claims priority from United States provisional application Serial
No. 60/076,770. filed March 4. 1998, the contents of which are hereby
incorporated by reference.
Field of the Invention
The present invention provides a solid dosage formulation of topiramate
and process for producing the solid dosage formulation. More particularly, the
solid dosage formulation comprises core particles which are coated with a taste
mask coating to provide coated particles which can be sprinkled onto food to ease
administration to patients who have difficulty swallowing tablets or capsules, e.g.,
pediatnc patients.
Background of the Invention
The pnarmaceutical industry employs a variety of dosage formulations for
orally administering medicinal agents to patients. Typical formulations for oral
administration include liquid solutions, emulsions, or suspensions, as well as sotid
forms such as capsu.es or tablets (as used herein, the term "tablet" means any
shaped and compressed solid dosage form, including caplets). Since these
conventional solid dosage formulations are usually intended for adults who can
easily swallow large tablets whole, the often disagreeable taste of the active
ingredient need not be taken into account in formulating the medicine, except for
the provision of means to prevent the taste from being apparent during the short
time that the medicine is in the mouth. Such means may include the provision of
an appropriate coating on the tablet, the use of a capsule form (the gelatin outer
shell of the capsule keeps the active ingredient inside until the capsule has been
swallowed) or smoky firmly compressing a tablet so that it will not begin to
disintegrate during the short time that it is intended to be in the mouth.
Children, older persons, ana many other persons have difficulty swallowing
whole tablets and even capsules. Therefore, it is often desirable to provide the
medicine either in liquid form or in a chewable solid form or an alternative solid
form, e.g., small particles which can be sprinkled onto soft food and swallowed
intact with the food, in addition to tne tablet or capsule intended to be swallowed
whole. Even where the medicine can be formulated as a liquid, it is desirable to
provide a chewabie solid form or an alternative solid form such as microspheres
which can be sprinkled onto soft food (e.g., baby food) because it is often more
convenient and easier to administer.
A major requirement of any such solid form is that it must be palatable,
since an unpalatable formulation greatly increases the risk of a patient neglecting
to take a medication. A further requirement of any solid dosage form is that it
must be bioavailable; that is, once the formulation reaches the stomach, the
individual particles should release the active ingredient rapidly and completely to
ensure that substantially ail of the active ingredient is absorbed. In cases where
the active ingredient is particularly unpalatable and somewhat unstable, it may be
difficult if not impossible, to identify a solid form that fulfills both of these
requirements (i.e., palatable and broavailable).
A number of references are known which describe pharmaceutical
compositions of unpalatable medicinal agents which are coated with a taste
masking coating in order to hide the unpleasant taste. Julian et al., in U.S. Patent
No. 4,851,266, describe chewable medicament tablets made by coating granules
of a medicament (especially, acetyl p-aminophenol) with a blend of cellulose
acetate or cellulose acetate butyrate and polyvinyl pyrrolidone (also known as
"PVP" and referred to hereinafter by its United States Pharmacopeia (USP) name
as "povidone"). Mehta, in U.S. Patent No. 5,084,278, discloses a pharmaceutical
composition composed of a pharmaceutical core of an active dose of a compound
and a rnicroencapsulating polymer which coats the pharmaceutical core and is
capable of taste-masking tne active compound. Bhardway, et al., in U.S. Patent
No. 5.578,316. describe medicament cores coated with methacryiate ester
capolymers which mask the bitter and unpleasant taste of the medicament
A variety of chlorosulfate and sulfamate esters of 2,3:4,5-bis-O-(1 -
methylethylidene)-ß-D-fructopyranose and their anticonvulsant activity in
mammals, ana thus their utility in treating diseases such as epilepsy and
glaucoma, are described in U.S. Patent No. 4,513,006. More specifically, the
compound 2,3:4,5-bis-O-(1-methylethylidene)-ß-D-fructopyranose sulfamate.
hereinafter referred to as "topiramate", is presently available for marketing as a
tablet product in strengths of 25, 50,100, 200, 300 and 400 mg as adjunctive
therapy for the treatment of adults with partial onset seizures (TOPAMAX®
(topiramate) tablets). Topiramate can be prepared following the processes
disclosed in U.S. Patent Nos. 4,513,006 and 5,387,700, and preferably, by the
process described in Examples 1 to 3 of U.S. Patent No. 5,387,700. Difficulty in
identifying a chewable solid form of topiramate has ensued due to the extremely
bitter taste of topiramate and problems associated with stability of the active agent,
especially upon exposure to moisture and heat which are known to cause
degradation of topiramate Degradation of topiramate is readily detected by
changes in physical appearance, i.e.. discoloration to brown or black, and by the
formation of sulfate ions which can be readily detected by standard techniques
know to those of ordinary skill in the an (e.g. HPLC).
Accordingly, it is an object of the invention to provide a stable solid
formulation of topiramate for use in children and other patients who have difficulty
swallowing conventional solid forms (e.g., tablets, capsules) which is both
palatable and bioavailable it is a further object of the invention to provide a
palatable solid formulation of topiramate that can be sprinkled onto soft food prior
to consumption (i.e., a "sprinkle formulation") and which provides immediate
release of the active ingredient in the stomach.
Summary of the Invention
The present invention is directed to a process for forming a pharmaceutical
composition comprising:
(a) prepanng core particles comprising an active agent of topiramate;
(b) drying the core particles from step (a) to form dried core particles;
(c) coating the dried core particles from step (b) with a taste masking
mixture to form coated particles; and
(d) drying the coated particles from step (c) to form the pharmaceutical
composition wherein the amount of taste masking mixture ranges from about 7%
by weight to about 15% by weight of the pharmaceutical composition, preferably,
about 9 to about 13%, and most preferably, about 11 % by weight of the
pharmaceutical composition.
In another aspect of the invention is a pharmaceutical composition
comprising:
(a) core particles containing an active agent of topiramate, wherein the core
particles have an initial particle size between about 0.100 mm and 2.5 mm; and
(b) a taste mask coating, wherein the taste mask coating comprises
between about 7% by weight and about 15% by weight of the pharmaceutical
composition, preferably, about 9 to about 13%, and most preferably, about 11% by
weight of the pharmaceutical composition and wherein the coated partides of the
pharmaceutical composition have a final particle size of about 0.100mm to about
2.5 mm
In one embodiment of the invention, the core partides comprise the active
agent of topiramate and at least one excipient preferably, the core particles
comprise the active agent of topiramate, a binder and a diluent; more preferably,
the core partides comprise the adive agent of topiramate, a binder and sugar
spheres.
In a class of the invention is a pharmaceutical composition comprising
about 85 to about 93% by weight core beads, arc about 7 to about 15% by weight
of a coating; wherein the core beads comprise about 18 to about 21 % by weight of
topiramate, about 8 to about 11% by weight of povidone. and about 58 to about
51% by weight of sugar spheres; and the coating comprises about 6 to about 9%
by weight of cellulose acetate, and about 2 to about 5% by weight of povidone.
In a subclass of the invention is the pharmaceutical composition comprising
about 89% by weight of core beads and about 11 % by weight coating, wherein the
core beads comprise about 19.8% by weight topiramate. about 9.9% by weight
povidone, and about 59.3% by weight sugar spheres; and the coating comprises
about 7.2% by weight cellulose acetate and about 3.8% by weight povidone.
Illustrative of the invention are methods of treating convulsions and/or
epiiepsy in a mammal in need thereof which comprises administering to the
mammal a therapeutically effective amount of any of the pharmaceutical
compositions of the present invention.
Also included in the invention are methods of treating a condition selected
from neuropathic pain, amyotrophic lateral schlerosis, acute ischemia, obesity,
diabetes, psoriasis or bipolar disorder (including manic depression) in a mammal
in need thereof which compnses administenng to the mammal a therapeutically
effective amount of any of the pharmaceutical compositions of the present
invention.
Detailed Description of the Invention
The present invention provides a solid dosage formulation of topiramate
intended primanly for pediatnc use or for patients who cannot swallow tablets.
More particularly, the solid dosage formulation is a sprinkle formulation comprising
core particles of the active agent which is taste-masked with a second layer to
obscure the extremely bitter taste of topiramate. The core particles can compnse
topiramate alone, e.g., in granular or crystalline form, or topiramate and one or
more excipients which are then formed into granules or beads by techniques
known to one of ordinary skill in the art e.g., roller compaction and comminution,
extrusion-spheronization or other methods of forming granules or beaas. The
preferred solid dosage formulation of the present invention is in the form of
microspheres which may be sprinkled onto soft food (e.g., baby food) and
swallowed by the patient along with the food.
In a preferred embodiment, three strengths, 15, 25, and 50 mg, are
obtained from a single sprinkle formulation of topiramate coated onto sugar
spheres using povidone as a binder, and taste-masked with a coating of cellulose
acetate and povidone to form coated beads. The strengths are differentiated by
means of diffenng fill weights and of proportional capsule sizes. That is, to aid in
delivery of the appropriate dosage to the patient, an amount of coated beads
sufficient to deliver the desired dose may be encapsulated into a capsule, for
example, a size 0, size 1, or size 2 gelatin capsule consisting of a white body with
a natural cap. Black pharmaceutical ink can be utilized to provide product
identification information on the capsules. For pediatric patients, the capsules can
be opened and the contents of the capsules sprinkled onto food and ingested;
however, mature patients may swallow drug product in intact capsules, if desired.
In general, the process for the preparation of the spnnkle formulation
includes a step in which core parades comprising granules, beads or crystals of
topiramate, alone or in combination with one or more excipients are coated with a
taste masking mixture and then dried. The term "particles"" as used herein refers
to free flowing substances of any shape which are larger than a powder including
crystals, beads (smooth, round or spherical particles) and granules. A variety of
methods known to those of ordinary skill in the art of pharmaceutical sciences may
be employed to prepare the core particles comprising the active agent of
topiramate. In one method, granules or large single crystals of topiramate can be
utilized as the core particles and coated with the taste masking mixture. The
coated material formed from the granules or crystals of topiramate may then be
compressed into chewable tablets, if desired or sprinkled onto soft food and
swallowed.
In a second approach, the active agent cf tociramate (in powder form) is
first placed in a fluidized bed equipment and thereafter, a spray binder solution or
suspension compnsed of, for example, povidone. siarch, sugar, syrup, HPMC
among other excipients known to those of ordinary skill in the art in a
pharmaceutically acceptable solvent (e.g., water, ethanol, acetone, among others)
is sprayed onto the powder, formed into granules and then dried until the solvent is
evaporated to provide the core particles. The drying temperature may vary over a
broad range, but should not be so high as to render the active agent inactive As a
slight modification of this second approach, a suspension of topiramate and a
binder in a pharmaceutically acceptable solvent is sprayed onto sugar spheres in
a fiuidized bed equipment and dried to provide core beads.
In a third method for forming the core particles, powdered or granular active
agent, and diluent or bulking agent are mixed with water or a pharmaceutically
acceptable solvent (e.g., water, ethanol) to form a wet mass. The mixture is mixed,
e.g., in a Hobart mixer or other suitable mixer, until a wet mass or dough is formed.
The wet mass is then placed in an extruder and extruded as a long thin strand.
The mixture may then be dried and suitably comminuted or may be placed in a
suitable spheronizer to make a pharmaceutical core that is round followed by
drying. The drying temperature may vary over a broad range, but should not be so
high as to render the active agent inactive.
Still another approach for forming the core particles is by roller compaction
of topiramate, either alone or in combination with one or more excipients. For
example, topiramate in powdered or granular form can be mixed with excipient to
provide suitable binding and lubricity, for example microcrystalline cellulose.
magnesium stearate or talc among others, and then passed through a compactor
to compact the mixture into a mass. The mass is then passed through a size
reduction machine and reduced to a suitable particle size to provide the core
panicles.
As used herein, the term "topiramate" and "active agent of topiramate" are
synonymous and are used interchangeably throughout the specification to refer to
the compound 2,3:4,5-bis-O-(1-methylethylidene)-ß- fructopyranose sulfamate
which forms the active agent of the pharmaceutical compositions of the present
invention. Topiramate and its use for treating epilepsy and glaucoma are
described in U.S. Patent No. 4.513,006. Topiramate can be synthesized
according to the processes disclosed in U.S. Patent Nos. 4,513,006 and
5,387,700, and preferably, according to the process of Examples 1-3 of U.S.
Patent No. 5,387,700.
The term "therapeutically effective amount" as used herein means that
amount of active compound or pharmaceutical agent that elicits the biological or
medicinal response in a tissue, system, animal or human that is being sought by a
researcher, veterinarian, medical doctor or other clinician, which includes
alleviation of the symptoms of the disease being treated.
The term "excipient," as used herein, refers to any inert substance which
may be combined with an active agent for preparing convenient dosage forms,
including, for example, diluents, binders, lubricants, disintegrants. colors, flavors
and sweeteners.
Suitable diluents for use in the formulation and processes of the present
invention include, but are not limited to, dicalcium phosphate, calcium sulfate,
lactose,sorbitol, microcrystalline cellulose, kaolin, mannitol, sodium chloride, dry
starch, powdered sugar and sugar spheres. In a preferred embodiment of the
invention, sugar spheres (20-60 mesh, preferably, 20-40 mesh, most preferably,
20-24 mesh) are utilized as a diluent in the core beads. In a particularly preferred
embodiment, sugar spheres NF (20/25 mesh) available from Crompton & Knowles
Corporation as NU-PAREIL PG® are used.
Suitable binders for use in the instant formulation and processes include,
but are not limited to synthetic gums such as hydroxypropyl methylcellulose
("HPMC"), povidone, carboxymethylcellulose, ethylcellulose and methyl-cellulose,
starch, pregelatinized starch, geiatin, sugars (e.g., molasses) and naturae gums
(e.g., acacia gum. sodium alginate, panwar gum). Preferably, povidone
(especially, Povidone USP) is used as the binder. In a particularly preferred
embodiment, the povidone is PLASDONE® (K29/32) supplied by ISP
Technologies, Inc. as a manufacturer of GAF products.
Disintegrants which can be utilized in the formulation and processes of the
present invention include, but are not limited to, methylcellulose, cellulose,
carboxymethylcellulose, croscarmellose sodium, magnesium aluminum silicate,
povidone, starch, sodium starch glycolate, pregelatinized starch, alginic acid and
guar gum. Preferably, the disintegrant is povidone. In a particularly preferred
embodiment, the povidone is PLASDONE® (K29/32) supplied by ISP
Technologies, Inc. as a manufacturer of GAF products.
Suitable taste masking agents which can be used in the formulation and
processes include, but are not limited to, cellulose acetate, cellulose acetate
butyrate, ethylcellulose. methylcellulose (including ethylcellulose and
methylcellulose combinations), and a wide range of copolymers available under
the tradename of Eudragits (Rohm Pharma of Darmstadt Germany). In a
preferred embodiment the taste masking agent s cellulose acetate (Cellulose
Acetate, NF).
A variety of solvents may be used as the first and second solvent in the
processes for preparing the pharmaceutical composition. Suitable solvents
include, but are not limited to, water, acetone, alcohols (e.g., methanol, ethanol,
isopropanol), methylene chloride, ethyl acetate, methyl ethyl ketone, and mixtures
thereof. In a preferred embodiment, the first solvent used for forming the core
beads is water, and the second solvent used for coating the core beads with the
taste masking mixture is an acetone-alcohol mixture, preferably, an acetone-
ethanol mixture, more preferably. an acetone-dehydrated alcohol mixture.
In a preferred embodiment, a suspension of topiramate ana a binder in a
first solvent is sprayed onto sugar spneres (20-25 mesh) and dried to provide core
beads. The core beads are then screened to remove fines and agglomerates.
The core beads are coated again with a taste masking mixture and then dried.
The taste masking mixture, which is sprayed onto the core beads, compnses a
taste masking agent and a disintegrant dissolved or suspended in a second
solvent, which may be the same or different from the first solvent. Coated beads
are sifted to remove fines and agglomerates, prior to encapsulation.
In a particularly preferred embodiment of the process for preparing the
sprinkle formulation, a suspension of topiramate in a solution of povidone in
purified water is sprayed onto sugar spheres (20-25 mesh) and dried in a fluid bed
processor equipped with a Wurster column. The ratio of topiramate: povidone
utilized in the suspension can be 50:25, 50:30 or 50:35. Preferably, a 50:25 ratio
of topiramate povidone is used. The core beads then are screened to remove
fines and agglomerates such that the core beads have a particle size between
about 0.100 mm and about 2.5 mm, preferably, between about 0.5 mm and about
1.5 mm, most preferably, between about 0.710 mm and about 1.18 mm. The core
beads are coated again with a taste masking mixture of cellulose acetate and
povidone suspended in an acetone/alcohol mixture in a fluid bed unit equipped
with a Wurster column, and dried. The ratio of cellulose acetate/povidone in the
taste masking mixture can be 60/40. 50/50, 65/35 or 55/45, preferably, a 65/35
ratio of cellulose acetate/povidone is utilized. Coated beads are sifted to remove
fines and agglomerates to provide a final particle size between about 0.100 mm
and about 2.5 mm, preferabiy. between about 0.5 mm and about 1.5 mm, most
preferaably, between about 0.850mm and about 1.18 mm. The coated beads are
packaged (e.g., in capsules, sachets or other methods known to those of ordinary
skill in the art) to deliver the desired amount of active ingredient to the patient.
When a particle size range is specified for the core and/or coated particles
(e.g., between about 0.100 mm and about 2.5 mm), it is intended that at least 75%.
preferably, 85%, and most preferaDly, 95% of the particles have a particle size
falling within the specified range (e.g., about 0.100 mm and about 2.5 mm).
The invention will be described more specifically in terms of its preferred
embodiment which is the preparation of a sprinkle formulation of topiramate. In
the first step of the process, core beads are prepared by coating sugar spheres
(20-25 mesh) with a suspension of topiramate and povidone in water. More
particuiaf1y, the sugar spheres are placed in a fluidized bed coater and fluidized by
a flow of warm air. The temperature of the air has not been found to be narrowly
critical, and can vary over a wide range, however, the temperature should not be
high enough to cause decomposition, sintering, or melting of the sugar spheres.
When coating the sugar spheres with the topiramate/povidone suspension
(preferably, a 50:25 ratio), a temperature from about 50° to 75°C has been found
to be suitable. The rate of air flow is adjusted so as to fluidize the sugar spheres.
Such flow will vary depending on factors such as the specific equipment used, the
size of the individual sugar spheres, the size of the charge of sugar spheres, the
apparent specific gravity of the spheres, and other factors known to the worker in
the arts relating to fluidized bed coating. After the sugar spheres have been
fluidized, a previously prepared suspension of topiramate in a solution of povidone
in water is sprayed onto the fluidized bed to provide the core beads. The air flow
through the bed is continued until the amount of water remaining in the topiramate
core beads has been substantially reduced. The core beads are-actually dry to
1ne touch within a very short tone after the topiramate suspension has been
sprayed onto the sugar spheres. However, the total drying time required to ensure
that the water content has been reduced to the desired level may take much
longer, depending on the temperature of the air, the size of the batch and the like
Routine experimentation will suffice to determine the appropriate ar temperatures
and total times required in the fluidized bed coaters in individual cases. The core
beads are sized through a sifter using 16 mesh and 25 mesh screens.
In the second step of the process, the core beads are coated with a taste
masking mixture to provide the coated beads of the sprinkle formulation. More
specifically, the core beads are placed in a fluidized bed coater and fluidized by a
flow of warm air. The temperature of the air nas not been found to be narrowly
critical, and can vary over a wide range, keeping in mind the fact that the
temperature should not be so high as to cause decomposition, sintering, or
melting, of the topiramate core beads. When coating the topiramate core beads, a
temperature of from 30° to 75°C has been found to be suitable. The rate of air
flow is adjusted so as to fluidize the core beads. Such flow will vary depending on
factors such as the specific equipment used the size of the charge of core beads,
the size of the individual core beads, the apparent specific gravity of the core
beads, and other factors known to the worker skilled in the arts of fluidized bed
coating. After the core beads have been fluidized, a taste mask coating mixture is
sprayed onto the fluidized bed. The taste mask coating mixture comprises a
solution of cellulose acetate/povidone (preferably, in a 65:35 ratio) in an acetone-
alcohol (preferably, acetone-dehydrated alcohol) solvent mixture. The air flow
through the bed is continued until the amount of solvent remaining in the coating
has been reduced to part per million levels. The coated beads are actually dried
to the touch within a very short time after the coating solution has been sprayed
onto the topiramate core beads. However, the total drying time required to ensure
that the solvent content of the coating has been reduced to the level desired may
take much longer, depending on the temperature of the air, the size of the batch
and the like. Routine experimentation will suffice to determine the appropriate air
temperature and total times required in the fluidized bed coalers in individuals
cases. The coated beads are then sized through a sifter using 16 mesh ana 20
mesh screens.
A sprinkle formulation having satisfactory taste masking and bioavailability
properties was obtained when the taste mask coating comprises about 7 to about
15% by weight of the final pharmaceutical composition. Preferably the taste mask
coating comprises about 9% by weight to about 13% by weight, most preferably,
about 11 % by weight, of the pharmaceutical composition when dried.
Dissolution results in water indicative of bioavailability for the
Dnarmaceutical composition having between 7 and 15% by weight taste mask
coating are shown below in Table 1.
To aid in delivery of the appropriate dosage to the patient, an
encapsulation machine can be utilized to encapsulate an amount of coated beads
to provide 15 mg, 25 mg and 50 mg strengths of topiramate into a size 2,1 or 0
gelatin capsule, respectively.
While the use of fluidized bed coating has been described in some detail
as one preferred method for making the core beads and the coated beads, other
techniques for making the core and coated beads readily known to those of
ordinary skill in the art may be used. Such other techniques include various
microencapsulation techniques such as coacervation and solvent evaporation.
In a particularly preferred embodiment, the ingredients and amounts of
each ingredient used to prepare the topiratmate sprinkle bead formulation are
provided in Table 2.
The strengths of toptramate sprinkle capsules, 15, 25 and 50 mg are
obtained from a single formulation of topiramate-coated beads by encapsulating
the proportionate amounts of coated beads in appropnately sized and marked
capsules. Table 3 provides a batch formula for a production batch of topiramate
sprinkle bead formulation.
A comparison of dissolution rates in water between TOPAMAX® 100 mg
tablets and topiramate sprinkle capsule formulations, 25 and 50 mg dosages
{according to the specifications of Table 2) are shown in Table 4
The stability of the sprinkle formulation of the present invention was
compared to TOPAMAX® (topiramate) tablets by storing both formulations in
controlled stability chambers for the purpose of determining the stability profile for
the two products. Samples were stored at 30°C. The sprinkles were stored at
60% relative humidity (RH); relative humidity for the tablet batches was either
controlled at 35% RH or was not controlled, but, in any event, was well below 60%
RH. Data were collected for assay (amount of drug remaining), sulfate and
sulfamate. physical appearance at selected time intervals, e.g., 18 months, 24
months. Physical appearance i.e. discoloration to brown or black, and amount of
sulfate detected are good indicators of degradation of the active agent
(topiramate) For each mote of topiramate that degrades, a molar equivalent of
inorganic impurity (sulfate/sulfamate) is formed. The presence of inorganic
impurity is readily determined by one of ordinary skill in the art using standard
techniques, e.g.. HPLC.
At 18 months, some instability was detected by appearance data for the
tablets, while the sprinkle formulation showed no signs of instability/degradation.
Clear signs of degradation were apparent by appearance and sulfate data for the
tablets at 24 months. After 24 months of storage at 30 degrees 60% RH, the 25
and 50 mg strengths of sprinkle capsules remained stable while the 15 mg
strength showed instability. At 25 degrees 60% RH storage for 24 months, all
three strengths of the sprinkle formulation remained stable.
It is known that moisture accelerates the degradation of topiramate. It has
now been unexpectantly found that the coating used to taste mask the topiramate
core beads also provides a barrier to the absorption of moisture, and therefore,
improves on the stability of the spnnkle forrnuiation. For storage of the tablets, it
was necesssary to put a desiccant into the bottles to stabilize the tablet
formulation. However, there is no need for a dessicant for the sprinkle formulation.
In addition, the capsules which are used to ease delivery of the appropriate
dosage of sprinkles contain more than 10% moisture by weight, and yet, this
moisture does not accelerate the degradation of topiramate because of the taste
mask coating for the sprinkles.
The following examples are provided to further define the invention without
however, limiting the invention to the particulars of these examples.
Batch amounts of each of the core bead ingredients were accurately
weighed out. in a jacketed kettle (approximately 50 gallons) equipped with a
sweeper, a homogenizer (Silverson or equivalent) and a mixer (L1GHTNIN1® or
equivalent) was placed the appropriate batch amount of purified water. USP The
batch amount of Povidone, USP was added and the resulting mixture mixed for a
minimum of 15 minutes to disperse the povidone in the purified water. The
topiramate (37.50kg) was added and the mixture mixed for a minimum of 15
minutes to disperse. Water was passed through the jacket. Using the mixer and
homogenizes the topiramate suspension was homogenized for approximately 90
minutes (range: 80-100 minutes). Stirring was continued through the steps which
follow for preparing the core beads.
A pump (Masterflex or equivalent) was prepared with three pump heads for
spraying. The batch quantity of sugar spheres, NF was charged to a fluid bed
(Glatt Fluid Bed equipped with a 32 inch Wurster column, 3 guns with 2.2 mm
nozzles, or equivalent) The sugar spheres were fluidized and the topiramate
suspension sprayed through the nozzles (approximate spray rate: 1 kg/min;
approximate spray time: 2.25 hours) according to the parameters shown in Table
5.
The core beads were dried at 60°C for at least 15 minutes (range: 15-18
minute) after the bed temperature had reached 60°C (range: 55°C-65°C)
according to the parameters provided in Table 6.
The core beads were then sized through a 48" sifter (Sweco or equivalent),
using 16 mesh and 25 mesh screens to remove fines and agglomerates
The batch quantities of Acetone, NF and Dehydrated Alcohol. USP were
transferred to a suitable stainless steel tank and-mixed. The natch quantity of
Povidone, USP was added using a suitable mixer (LIGHTNIN® or equivalent).
The batch quantity of Cellulose Acetate, NF was added at the vortex while mixing
with a suitable mixer and the coating solution was checked visually for clarity.
The 16/25 mesh topirarnate core beads (150 kg) from Example 1 were
fluidized in a Glatt Fluid Bed processor equipped with a Wurster column (or
equivalent). The core beads were sprayed with the coating solution until the entire
quantity of coating solution was exhausted. The coated beads were dried at
approximately 60°C for a minimum of 30 minutes (range 23-32 minutes).
Operating parameters are shown in, Table 7.
A Sweco Sifter (or equivalent equipment) was fitted at the top with a 16
mesh screen and at the bottom with a 20 mesh screen. The entire batch of coated
beads was sieved and coated beads outside the 16-20 mesh range discarded.
Example 3
Encapsulation of Coated Beads
An encapsulation machine (H&K Encapsulator or equivalent) was prepared
with a bead filter attechment and the coated beads from Example 2 encapsulated.
Target fit weights were determined by assay of the coaled beads prior to
encapsulation. Variability of the fill weight was controlled by weight sorting, which
is required for the 15 mg strength, but optional and employed asnecessary for the
25 and 50 mg strengths A KKE sortng machine (or equivalent was used to
weigh the filled capsules when weight sorting was employed. Filled capsules not
meeting the acceptable weight range were discarded by the sorter.
While the foregoing specification teaches the principles or the present
invention, with examples provided for the purpose of illustration will be
understood that the practice of the invention encompasses all of the usual
variations, adaptations and/or modifications as come within the scope of the
following claims and their equivalents.
WE CLAIM:
1. A process for forming a pharmaceutical composition comprising:
a) preparing core particles comprising an active agent of topiramate;
b) drying the core particles from step (a) to form dried core particles;
having a particle size of 0.100 mm to 2.5 mm;
c) coating the dried core particles from step (b) with a taste masking
mixture to form coated particles; and
d) drying the coated particles from step ( c) to form the pharmaceutical
composition wherein the amount of taste masking mixture ranges
from 7% by weight to 15% by weight of the pharmaceutical
composition, and the coated particles have a final particle size of
0.100 mm to 2.5mm.
2. The process as claimed in claim 1, wherein the core particles comprise
the active agent of topiramate and at least one excipient.
3. The process as claimed in claim 2, wherein the core particles comprise
the active agent of topiramate, a binder and a diluent wherein the diluent
is sugar spheres.
4. The process as claimed in claim 3, wherein the taste masking mixture
comprises 9 to 13% by weight of the pharmaceutical composition.
5. The process as claimed in claim 1, wherein the core particles are
prepared by spraying a suspension of topiramate and the binder in a
solvent onto the sugar spheres.
6. The process as claimed in claim 5, wherein the binder is selected from
povidone, HPMC, acacia gum, sugar, molasses, sodium alginate, panwar
gum, starch, pregelatinized starch, carboxymethylcellulose, ethylcellulose
or methylcellulose.
7. The process as claimed in claim 6, wherein the binder is povidone.
8. The process as claimed in claim 6, wherein the taste masking mixture
comprises a taste masking agent selected from cellulose acetate,
cellulose acetate butyrate, methylcellulose, ethylcellulose or a Eudragit;
and a disintegrant selected from povidone, methylcellulose, starch,
sodium starch glycolate, pregelatinized starch, cellulose,
carboxymethylcellulose, croscarmellose sodium, magnesium aluminate
silicate, alginic acid or guar gum.
9. The process as claimed in claim 8, wherein the taste masking mixture
comprises cellulose acetate and povidone.
10.The process as claimed in claim 9, further comprising encapsulating the
coated bead.
11. A pharmaceutical composition comprising
a) core particles containing an active agent of topiramate, wherein the
core particles have an initial particle size between 0.100mm and
2.5mm; and
b) a taste mask coating, wherein the taste mask coating comprises
between 7% by weight and 15% by weight of the pharmaceutical
compostion and wherein the coated particles of the pharmaceutical
composition have a final particle size of 0.100 mm to 2.5 mm.
12.The pharmaceutical composition as claimed in claim 11, wherein the core
particles comprise the active agent of topiramate and at least one
excipient.
13.The pharmaceutical composition as claimed in claim 12, wherein the core
particles comprise the active agent of topiramate, a binder and a diluent
wherein the diluent is sugar spheres.
14.The pharmaceutical composition as claimed in claim 13, wherein the taske
mask coating comprises between 9% by weight and 13% by weight of the
pharmaceutical composition.
15.The pharmaceutical composition as claimed in claim 14, wherein the taste
mask coating comprises 11% by weight of the pharmaceutical
composition.
16.The pharmaceutical composition as claimed in claim 15, wherein the core
particles have an initial particle size between 0.5 mm and 1.5 mm and the
coated particles of the pharmaceutical composition have a final particle
size between 0.5 mm and 1.5mm.
17.The pharmaceutical composition as claimed in claim 16, wherein the core
particles have an initial particle size between 0.710 mm and 1.18 mm and
the coated particles of the pharmaceutical composition have a final
particle size between 0.850 mm and 1.18mm.
18. The pharmaceutical composition as claimed in claim 17, wherein the
binder is selected from povidone, HPMC, sodium alginate, panwar gum,
acacia gum, gelatin, sugar, molasses, starch, methycellulose,
ethylcellulose or caroboxymethylcellulose; and the taste mask coating
comprises a taste masking agent and a disintegrant, wherein the taste
masking agent is selected from cellulose acetate, methylcellulose,
ethylcellulose, a Eudragit or cellulose acetate butyrate; and the
disintegrant is selected from povidone. cellulose, carboxymethylcellulose,
croscarmellose sodium, magnesium aluminate silicate, starch, sodium
starch glycolate, pregelatinized starch, alginic acid or guar gum.
19.The pharmaceutical composition as claimed in claim 18, wherein the
binder is povidone, the taste masking agent is cellulose acetate and the
disintegrant is povidone.
20.The pharmaceutical composition as claimed in claim 19, wherein the
coated particles of the pharmaceutical composition are encapsulated.
21. The pharmaceutical composition comprising 85 to 93% by weight core
beads and 7 to 15% by weight of a coating; wherein the core beads
comprise 18 to 21% by weight of topiramate, 8 to 11% by weight of
povidone and 58 to 61% by weight of sugar spheres; and the coating
comprises 6 to 9% by weight of cellulose acetate and 2 to 5% by weight of
povidone.
22.The pharmaceutical composition as claimed in claim 21, comprising 89%
by weight of core beads and 11% by weight coating, wherein the core
beads comprise 19.8% by weight topiramate, 9.9% by weight povidone,
and 59.3% by weight sugar spheres; and the coating comprises 7.2% by
weight cellulose acetate and 3.8% by weight povidone.
A process for forming a pharmaceutical composition comprising: a) preparing
core particles comprising an active agent of topiramate; b) drying the core
particles from step (a) to form dried core particles; having a particle size of 0.100
mm to 2.5 mm; c) coating the dried core particles from step (b) with a taste
masking mixture to form coated particles; and d) drying the coated particles from
step (c) to form the pharmaceutical composition wherein the amount of taste
masking mixture ranges from 7% by weight to 15% by weight of the
pharmaceutical composition, and the coated particles have a final particle size of
0.100 mm to 2.5mm.

Documents:

IN-PCT-2000-238-KOL-FORM-27.pdf

in-pct-2000-238-kol-granted-abstract.pdf

in-pct-2000-238-kol-granted-assignment.pdf

in-pct-2000-238-kol-granted-claims.pdf

in-pct-2000-238-kol-granted-correspondence.pdf

in-pct-2000-238-kol-granted-description (complete).pdf

in-pct-2000-238-kol-granted-form 1.pdf

in-pct-2000-238-kol-granted-form 18.pdf

in-pct-2000-238-kol-granted-form 2.pdf

in-pct-2000-238-kol-granted-form 26.pdf

in-pct-2000-238-kol-granted-form 3.pdf

in-pct-2000-238-kol-granted-form 5.pdf

in-pct-2000-238-kol-granted-letter patent.pdf

in-pct-2000-238-kol-granted-reply to examination report.pdf

in-pct-2000-238-kol-granted-specification.pdf

in-pct-2000-238-kol-granted-translated copy of priority document.pdf


Patent Number 218996
Indian Patent Application Number IN/PCT/2000/238/KOL
PG Journal Number 16/2008
Publication Date 18-Apr-2008
Grant Date 16-Apr-2008
Date of Filing 22-Aug-2000
Name of Patentee ORTHO-MCNEIL PHARMACEUTICAL INC.,
Applicant Address US ROUTE NO.202, RARITAN, NEW JERSEY 08869-0602
Inventors:
# Inventor's Name Inventor's Address
1 THAKUR, MADHAV S., 112 MENDHAM DRIVE, NORTH WALES, PENNSYLVANIA 19477
2 KOTWAL, PRAMOD, M. 145 CAMBRONNE CIRCLE, BLUE BELL, PENNSYLVANIA 19422
3 GIBBS, IRWIN. S., 144 ROY LANE , HUNTINGTON VALLEY, PA 19006
PCT International Classification Number A61K 9/00
PCT International Application Number PCT/US99/04449
PCT International Filing date 1999-03-01
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 60/076,770 1998-03-04 U.S.A.