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Patent 2586473 Summary

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(12) Patent: (11) CA 2586473
(54) English Title: UNIFORM DRUG DELIVERY THERAPY
(54) French Title: TRAITEMENT PAR ADMINISTRATION UNIFORME DE MEDICAMENTS
Status: Expired
Bibliographic Data
(51) International Patent Classification (IPC):
  • A61K 31/277 (2006.01)
  • A61K 9/22 (2006.01)
  • A61P 9/10 (2006.01)
  • A61P 9/12 (2006.01)
(72) Inventors :
  • AYER, ATUL DEVDATT (United States of America)
  • LAM, ANDREW (United States of America)
  • MAGRUDER, JUDY A. (United States of America)
  • HAMEL, LAWRENCE G. (United States of America)
  • WONG, PATRICK S.-L. (United States of America)
(73) Owners :
  • ALZA CORPORATION (United States of America)
(71) Applicants :
  • ALZA CORPORATION (United States of America)
(74) Agent: SMART & BIGGAR
(74) Associate agent:
(45) Issued: 2011-05-31
(22) Filed Date: 1997-03-20
(41) Open to Public Inspection: 1997-10-16
Examination requested: 2007-10-17
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
60/014,889 United States of America 1996-04-05

Abstracts

English Abstract

The invention disclosed pertains to a novel delivery system comprising an agent formulation and means for dispensing the agent formulation from the delivery system.


French Abstract

La présente divulgation se rapporte à un nouveau système d'administration qui comprend une formulation d'agent et des moyens d'administration de la formulation de l'agent par ledit système.

Claims

Note: Claims are shown in the official language in which they were submitted.



34
CLAIMS:

1. A dosage form for the delivery of verapamil
hydrochloride at a uniform rate comprising:

(a) a composition comprising a hydrophilic polymer
of less than 250 microns;

(b) a composition comprising verapamil
hydrochloride having a particle size equal to or less than
150 microns and in an amount of from 25 ng to 750 mg;

(c) a wall comprising a composition permeable to
the passage of fluid that surrounds the compositions of (a)
and (b); and

(d) means in the wall for delivering the verapamil
hydrochloride at a substantially uniform rate from the
dosage form;

wherein delivery of the verapamil hydrochloride is initiated
about four hours after contact with an aqueous environment.
2. A dosage form for the delivery of verapamil
hydrochloride at a uniform rate comprising:

(a) a composition comprising verapamil
hydrochloride having a particle size equal to or less than
150 microns and in an amount of 25 ng to 750 mg, and a
hydrophilic polymer of less than 250 microns;

(b) a coat that surrounds the composition in (a)
and comprising means for delaying release of verapamil
hydrochloride;

(c) a wall comprising a composition that surrounds
the coat; and


35
(d) means in the dosage form for delivering the

verapamil hydrochloride from the dosage form over time;
wherein delivery of the verapamil hydrochloride is initiated
about four hours about contact with an aqueous environment.
3. A dosage form for the delivery of verapamil
hydrochloride at a uniform rate comprising:

(a) a composition comprising verapamil
hydrochloride having a particle size equal to or less than
150 microns and a hydrophilic polymer of less than 250
microns;

(b) a displacement composition in contact with the
composition in (a) comprising a polymer that expands in the
presence of fluid for displacing the composition in (a) from
the dosage form;

(c) a wall that surrounds the composition in (a)
and the displacement composition, said wall being permeable
to the passage of fluid; and

(d) means in the dosage form for delivering the
verapamil hydrochloride at a substantially uniform rate over
time.

4. A dosage form for the delivery of verapamil
hydrochloride at a uniform rate comprising:

(a) a composition comprising poly(ethylene oxide)
having a particle size of less than 250 microns;

(b) a composition comprising verapamil
hydrochloride having a particle size equal to or less than
150 microns and in an amount of from 25 ng to 750 mg;


36
(c) a wall comprising cellulose acetate,
hydroxypropylcellulose and polyethylene glycol, said wall
being permeable to the passage of fluid that surrounds the
compositions of (a) and (b); and

(d) means in the wall for delivering the verapamil
hydrochloride at a substantially uniform rate from the
dosage form;

wherein delivery of the verapamil hydrochloride is initiated
about four hours after contact with an aqueous environment.
5. A dosage form for the delivery of verapamil
hydrochloride at a uniform rate comprising:

(a) a composition comprising verapamil
hydrochloride having a particle size equal to or less than
150 microns and in an amount of from 25 ng to 750 mg, and
poly(ethylene oxide) having a particle size of less than 250
microns;

(b) poly(vinylpyrrolidone) coat that surrounds the
composition in (a) and comprising means for delaying release
of verapamil hydrochloride;

(c) a wall comprising cellulose acetate,
hydroxypropylcellulose and polyethylene glycol that
surrounds the coat; and

(d) means in the dosage form for delivering the
verapamil hydrochloride from the dosage form over time;
wherein delivery of the verapamil hydrochloride is initiated
about four hours after contact with an aqueous environment.
6. A dosage form for the delivery of verapamil
hydrochloride at a uniform rate comprising:


37
(a) a composition comprising verapamil
hydrochloride having a particle size equal to or less than
150 microns and poly(ethylene oxide) having a particle size
of less than 250 microns;

(b) a displacement composition comprising
poly(ethylene oxide) in contact with the composition in (a)
and that expands in the presence of fluid for displacing the
composition in (a) from the dosage form;

(c) a wall comprising cellulose acetate,
hydroxypropylcellulose and polyethylene glycol that
surrounds the composition in (a) and the displacement
composition and is permeable to the passage of fluid; and

(d) means in the dosage form for delivering the
verapamil hydrochloride at a substantially uniform rate over
time.

7. The dosage form of any one of claims 1, 2, 4 and 6
wherein the amount of verapamil hydrochloride is 240 mg.

8. The dosage form of any one of claims 1 to 7
wherein the release rate of verapamil hydrochloride is
about 17 to 30 mg/hour in 4 to 9 hours.

9. The dosage form for the delivery of verapamil
hydrochloride of any one of claims 1 to 8 for the treatment
of angina and high blood pressure in a subject.

10. Use of the dosage form for the delivery of
verapamil hydrochloride of any one of claims 1 to 8 for the
treatment of angina and high blood pressure in a subject.
11. Use of the dosage form for the delivery of
verapamil hydrochloride of any one of claims 1 to 8 in the


38
manufacture of a medicament for the treatment of angina and
high blood pressure in a subject.

Description

Note: Descriptions are shown in the official language in which they were submitted.



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1
UNIFORM DRUG DELIVERY THERAPY

This is a divisional application of Canadian
Patent Application No. 2,249,637 filed March 20, 1997.
FIELD OF THE INVENTION

This invention pertains to a dosage form that provides a substantially
uniform delivery of drug over an extended period of time. More particularly,
the invention concerns a dosage form that provides a known and constant
drug release pattern for an indicated therapy. The invention relates also to
a dosage form that provides a controlled-constant and uniform delivery of
a known dose of drug over time.

BACKGROUND OF THE INVENTION

A critical need exists for a dosage form for the controlled and uniform
administration of a drug for therapy over time. Presently, in the practice of
pharmacy and medicine, a drug is administered in conventional
pharmaceutical forms, such as tablets and capsules. These conventional
forms deliver their drug by dumping and this leads to uneven dosing of drug,
to uneven blood levels of drug characterized by peaks and valleys, and
accordingly this does not provide controlled and uniform therapy over time.
The prior art provided dosage forms for continuous therapy.
For example, in United States Pat, No. 4,327,725 issued to Cortese
and Theeuwes, and in United States Pat. Nos. 4,612,008; 4,765,989;
and 4,783,337 issued to Wong, Barclay, Deters and Theeuwes, a dosage
form is disclosed that provides therapy by generating an osmotic pressure
inside the dosage form, The dosage form of these patents operate
successfully for delivering a drug for a preselected therapy. With the
delivery
of some drugs however, these dosage forms often exhibit erratic release
rate patterns, such as a nonuniform variation in the drug release rate,
and the dosage form can stop delivering a drug, that is, the dosage form
can shut-down intermittently.


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,V0 97/37640 PCT/US97/044 _
2
1 It is immediately apparent, in view of the above presentation, that an
2 urgent need exists for a reliable dosage form. The need exists for a dosage
3 form endowed with properties for delivering a drug at a substantial and
4 uniform rate over time. The need exists also for a dosage form substantially
free-of-deviation in its release-rate profile, that delivers the needed dose
of
6 drug with a reduced amount of drug left in the dosage form at the end of the
7 delivery period. It will be appreciated by those knowledgeable in the drug
8 dispensing art, that is novel and unexpected dosage form is made available
9 that provides a substantially uniform and known drug-release profile, free
of
the tribulations of the prior art, such a dosage form would represent an
11 advancement and a valuable contribution in the drug dispensing art.
12

13 OBJECTS OF THE INVENTION
14
Accordingly, in view of the above presentation, it is an immediate
16 object of the invention to provide a dosage form that delivers a drug in a
17 substantially uniform dose to a biological drug receiving environment over
18 an extended drug-delivery therapy time.
19 Another object of the invention is to provide a novel dosage form that
substantially avoids administering a drug in a nonuniform and varying rate
21 and therefore exhibits substantially the same dose-dispensing rate over
time.
22 Another object of the invention is to provide a dosage form that
23 delivers a predetermined and prescribed dose in the same manner over time
24 while simultaneously lessen the amount retained or the residual drug left
in
and not delivered from the dosage form.
26 Another object of the invention is to provide a drug composition of
27 matter comprising drug particles of 5 m to 150 m, micron, and hydrophilic
28 polymer particles of 5 m to 250 m, characterized by the drug particles
and
29 the hydrophilic polymer particles functioning together to provide a uniform


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3
1 and nonvarying rate of release of both substantially-free of a deviation and
2 substantially-free of a decrease in the rate of the release over time.
3 Another object of the invention is to provide a dosage form comprising
4 a membrane that surrounds a drug core comprising drug particles of 1 to
150 m and hydrophilic polymer particles of 1 to 250 m, particles which

6 are co-delivered from the dosage form through an exit formed by a process
7 selected from the group consisting of a drilled exit, a bioerosion exit,
s a leaching exit, a solubilizing exit, and an exit formed by rupture.
9 Another object of the invention is to provide a dosage form comprising
a membrane comprising a semipermeable composition that surrounds a core
11 comprising a drug layer comprising drug particles of 1 to 150 m and
polymer
12 particles of 1 to 250 m, and a displacement layer comprising an
13 osmopolymer-hydrogel that imbibes fluid, hydrates and increases in swelling
14 volume and thereby displaces the drug layer through an exit membrane
selected from an exit in the group consisting of an orifice, passageway, pore,
16 microporous channel, porous overlay, porous insert, micropore, microporous
17 membrane and porepassageway.
18 Another object of the invention is to make available a process for
19 providing a substantially uniform and substantially nonvarying drug
delivery
program from a dosage form, wherein the process comprises the steps of
21 selecting drug particles of 1 to 150 m, selecting hydrophilic polymer
particles
22 of 1 to 250 lam, blending the selected particles into a drug-polymer core,
and
23 surrounding the core with a membrane comprising means for delivering the
24 drug from the core in a substantially-uniform and substantially-nonvarying
rate
of release over a period of time up to 30 hours.
26 Another object of the invention is to provide a dosage form for
27 delivering a drug to human, wherein the dosage form comprises a drug
28 composition comprising 0.05 ng to 1.2g of drug having a particle size of
29 1 to 150 m, and a hydrophilic polymer having a particle size of 1 to 250
m,
a push composition that imbibes fluid and expands for pushing the drug


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4
composition from the.dosage form, a wall that surrounds the
drug and the push composition and is permeable to the
passage of fluid, an inner coat that surrounds the drug and
push compositions positioned between the inside surface of
the wall and the drug and push compositions for governing
fluid imbition into the drug and push compositions for 30
minutes to 4 hours and 30 minutes, and at least one exit
means in the wall for delivering the drug composition at a
uniform and nonvarying rate over time.

Other objects, features, and advantages of the
invention will be more apparent to those versed in the
dispensing art comprising medicine and pharmacy from the
following detailed specification taken in conjunction with
the accompanying claims.

According to another aspect of the present
invention, there is provided a dosage form for the delivery
of verapamil hydrochloride at a uniform rate comprising:
(a) a composition comprising a hydrophilic polymer of less
than 250 microns; (b) a composition comprising verapamil
hydrochloride having a particle size equal to or less than

150 microns and in an amount of from 25 ng to 750 mg; (c) a
wall comprising a composition permeable to the passage of
fluid that surrounds the compositions of (a) and (b); and
(d) means in the wall for delivering the verapamil
hydrochloride at a substantially uniform rate from the
dosage form; wherein delivery of the verapamil hydrochloride
is initiated about four hours after contact with an aqueous
environment.

According to still another aspect of the present
invention, there is provided a dosage form for the delivery
of verapamil hydrochloride at a uniform rate comprising:

(a) a composition comprising verapamil hydrochloride having


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4a
a particle size equal to or less than 150 microns and in an
amount of 25 ng to 750 mg, and a hydrophilic polymer of less
than 250 microns; (b) a coat that surrounds the composition
in (a) and comprising means for delaying release of

verapamil hydrochloride; (c) a wall comprising a composition
that surrounds the coat; and (d) means in the dosage form
for delivering the verapamil hydrochloride from the dosage
form over time; wherein delivery of the verapamil
hydrochloride is initiated about four hours about contact
with an aqueous environment.

According to yet another aspect of the present
invention, there is provided a dosage form for the delivery
of verapamil hydrochloride at a uniform rate comprising:

(a) a composition comprising verapamil hydrochloride having
a particle size equal to or less than 150 microns and a
hydrophilic polymer of less than 250 microns; (b) a
displacement composition in contact with the composition in
(a) comprising a polymer that expands in the presence of
fluid for displacing the composition in (a) from the dosage

form; (c) a wall that surrounds the composition in (a) and
the displacement composition, said wall being permeable to
the passage of fluid; and (d) means in the dosage form for
delivering the verapamil hydrochloride at a substantially
uniform rate over time.

According to a further aspect of the present
invention, there is provided a dosage form for the delivery
of verapamil hydrochloride at a uniform rate comprising:

(a) a composition comprising poly(ethylene oxide) having a
particle size of less than 250 microns; (b) a composition
comprising verapamil hydrochloride having a particle size
equal to or less than 150 microns and in an amount of from
25 ng to 750 mg; (c) a wall comprising cellulose acetate,
hydroxypropylcellulose and polyethylene glycol, said wall


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4b
being permeable to the passage of fluid that surrounds the
compositions of (a) and (b); and (d) means in the wall for
delivering the verapamil hydrochloride at a substantially
uniform rate from the dosage form; wherein delivery of the
verapamil hydrochloride is initiated about four hours after
contact with an aqueous environment.

According to yet a further aspect of the present
invention, there is provided a dosage form for the delivery
of verapamil hydrochloride at a uniform rate comprising:
(a) a composition comprising verapamil hydrochloride having
a particle size equal to or less than 150 microns and in an
amount of from 25 ng to 750 mg, and poly(ethylene oxide)
having a particle size of less than 250 microns; (b)
poly(vinylpyrrolidone) coat that surrounds the composition
in (a) and comprising means for delaying release of
verapamil hydrochloride; (c) a wall comprising cellulose
acetate, hydroxypropylcellulose and polyethylene glycol that
surrounds the coat; and (d) means in the dosage form for
delivering the verapamil hydrochloride from the dosage form
over time; wherein delivery of the verapamil hydrochloride
is initiated about four hours after contact with an aqueous
environment.

According to still a further aspect of the present
invention, there is provided a dosage form for the delivery
of verapamil hydrochloride at a uniform rate comprising:
(a) a composition comprising verapamil hydrochloride having
a particle size equal to or less than 150 microns and
poly(ethylene oxide) having a particle size of less than
250 microns; (b) a displacement composition comprising
poly(ethylene oxide) in contact with the composition in (a)
and that expands in the presence of fluid for displacing the
composition in (a) from the dosage form; (c) a wall
comprising cellulose acetate, hydroxypropylcellulose and


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4c
polyethylene glycol that surrounds the composition in (a)
and the displacement composition and is permeable to the
passage of fluid; and (d) means in the dosage form for
delivering the verapamil hydrochloride at a substantially
uniform rate over time.

According to a preferred embodiment of the
invention, the release of verapamil hydrocholoride is
initiated about four hours after contact with an aqueous

environment.
According to another preferred embodiment of the
invention, the release rate of verapamil hydrochloride is
about 17 to 30 mg/hr in 4 to 9 hours.

BRIEF DESCRIPTION OF THE FIGURES

Figure 1 illustrates the drug release rate variation with a drug
possessing a particle size of 2 to 900 microns in the presence of a polymer
possessing 25% and more of greater than 250 micron size.
Figure 2 illustrates the drug release rate variation from a dosage
form with a drug size of less than 150 micron in the presence of a polymer
possessing 25% and more of greater than 250 micron.
Figure 3 illustrates pronounced decrease in the variation of the
drug release rate when the dosage form comprises a drug size of less than
150 micron accompanied by a polymer size of less than 250 micron.
DESCRIPTION OF THE INVENTION

The following examples are illustrative of the invention and they
should not be considered as limiting the invention in any way, as these
examples and other equivalents thereof will became apparent to those


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`. j.97/37640 PCTIUS97/04495
1 versed in the dispensing art in the light of the present specification and
2 the accompanying claims.
3

4 EXAMPLE 1
5

6 A dosage form for delivering a drug orally to the gastrointestinal tract of
7 the drug receiving patient in need of the drug's therapy is prepared as
follows:
a first 5 mg of 135 p.m amlodipine besylate, a calcium channel blocker, is

9 blended with a 5% solution of poly(vinylpyrrolidone) of 30,000 number
average molecular weight available from General Aniline and Film
11 Corporation, New York, New York, in a fluid bed processor. Then, the
12 granulated product is combined with 7.5 mg of 235 m a poly (alkylene

13 oxide), a polyethylene oxide), of 175,000 number average molecular weight
14 available from the Union Carbide Corporation, Danbury, Connecticut, 0.5 mg
of sodium chloride and 0.02 mg a stearic acid, and blended to provide a
16 homogenous blend, by blending 35 rpm for 7 minutes. The homogenous
17 blend is compressed into a drug composition and surrounded with a wall
18 comprising a semipermeable composition and an exit forming agent.
19 The wall composition comprises 65 wt% cellulose acetate having an
acetyl content of 34% and a 30,000 number average molecular weight
21 dissolved in acetone:water, to which 1.8 wt% triacetin and 1.5 wt% sodium
22 chloride are added with stirring constantly. The drug composition is
sprayed
23 in a fluidized bed air suspension coater to provide 10% wt wall. The dosage
24 form is dried at 25 C for 18 hours. The dosage form releases the amlodipine
besylate in a nonvarying rate through microchannels formed by fluid leaching
26 of the sodium chloride in the gastrointestinal fluid of the patient.


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6
EXAMPLE 2
2
3 The procedure of the above example is followed in this example,
4 wherein in the present example the drug is selected from the group
consisting
of 5 mg of lisinopril indicated as an angiotensin converting enzyme inhibitor,
6 10 mg of buspirone hydrochloride indicated as an antianxiety drug, and 5 mg
7 of oxybutynin hydrochloride indicated for relief of bladder instability, and
8 wherein the lubricant is magnesium stearate and the semipermeable wall
9 comprises mannitol.
11 EXAMPLE 3
12

13 A dosage form for the osmotically and hydrokinetically controlled
14 release of a beneficial drug is made as follows: first, to a mixing bowl is
added 500 mg of the oral antibacterial ciprofloxacin hydrochloride of
16 125 microparticle size followed by the addition of 105 mg of sodium
17 carb oxymethylcel I u lose of 22,000 number average molecular weight of
18 135 micron sizes and the ingredients mixed for 3 to 5 minutes to yield a
19 homogenous mix. Next, 10 mg of 88 microcrystalline cellulose of 11,000
number average molecular weight is added to the mixing bowl and 0.05 mg
21 of drug delivery surfactant sodium lauryl sulfate added to the bowl and all
22 the ingredients mixed for 5 minutes. Then, an aqueous solution containing
23 7.5 mg of poly(vinylpyrrolidone) of 30,000 number average molecular weight
24 is added with mixing and the resulting mixture is passed through an
extruder
onto a small tray and let dry overnight. The granulation is dried for 5 hours
at
26 50 C and 0.03 mg of lubricant added with mixing for 1 minute. A solid fluid
27 imbibing osmotic care is prepared in tablet press with a concave punch.
28 Next, an internal subcoat, drug free, is prepared comprising 94 wt%
29 hydroxyethylcellulose of 90,000 number average molecular weight and 6 wt%
polyethylene glycol in distilled water is coated around the drug composition


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7

1 and the subcoated drug composition is dried for 1 hour at 45 C. Then, an
2 outer coat comprising a semipermeable composition and a pore-passageway
3 former is prepared by adding cellulose acetate of 39.43% acetyl content to a
4 cosolvent of methylene chloride and methanol to yield a solution effected by
stirring and warming. Next, the pore-former sorbitol is added to a cosolvent
of
6 water and methanol with mixing followed by adding polyethylene glycol to
7 produce the outer coating solution. Finally, the outer coating solution is
8 coated around the subcoat in a pan coater and then dried for 18 hours at
9 45 C in a forced air oven, to yield the desired dosage form. The dosage
form,
in operation in the gastrointestinal fluid of a human in need of drug therapy,
11 provides a uniform and nonvarying-order of drug release through exit
12 passageways of controlled porosity effected by the fluidic leaching of the
13 soluble pore-forming additive incorporated in the semipermeable outer coat.
14 The cooperation of the drug particles and the hydrophilic polymer particles
provides a viscous gel that pushes the drug through the exits at the
16 given rate.
17

18 EXAMPLE 4
19
The procedure of the above example is followed, with the proviso in
21 this example the therapeutic member is selected from the group consisting
of
22 40 mg of simvastatin for lowering cholesterol, 75 mg of venlafaxine
23 antidepressant, 20 mg of fluoxetine antidepressant, 20 mg of antianginal
24 nifedipine, 40 mg of lovastatin indicated for lowering cholesterol, 20 mg
of
enalopril maleate an angiotensin converting enzyme inhibitor, 120 mg of
26 diltiazem for managing calcium ion influx, 500 mg of ciprofloxacin
27 hydrochloride an antibacterial, 100 mg of sertraline hydrochloride an oral
28 antidepressant, 100 mg of cyclosporin an immunosuppresant, 1 mg of
29 terazosin hydrochloride an alpha-adrenoceptor blocker, 50 mg of sumatriptan
succinate a 5-hydroxytryptamine receptor agonist, 40 mg of pravastatin


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WO 97/37640 PCT/US97/0449
8
1 sodium a hypolipidemic, 500 mg of an anti-HIV-proteinase inhibitor such as
2 nelfinavir, saquinavir, indinavir, or ritonavir, an anti-HIV such as
zidovudine,
3 didanosine, or lamivudine, a reverse transcriptase inhibitor such as
loviride,
a an antiviral herpes such as fumciclovir or gancidovir, 10 mg of alendronate
sodium for treating osteoporosis, and 2.5 mg of conjugated estrogen

6 indicated for the treatment of vasomotor symptoms associated with
7 menopause, atrophic vaginitis and osteoporosis loss of bone mass.
8

9 EXAMPLE 5

11 A dosage form for the oral uniform and nonvarying release of a drug
12 to a biological drug receptor is manufactured as follows: first, 6000g of
13 verapamil hydrochloride, indicated for the treatment of angina and high
14 blood pressure, having nonuniform particle size distribution between
1 micron to 900 micron, 3047g of poly(ethylene oxide) having a number
16 average molecular weight of 300,000 and having 25% particles greater
17 than 250 micron, 500g of sodium chloride and 100g of poly(vinylpyrrolidone)
18 having a number average molecular weight of 40,000 are added to a
19 Freund Flo-Coater's bowl, a fluid bed granulator. The bowl is attached to
the Flo-Coater and the granulation process is initiated. Next, the dry powders
21 are air suspended and mixed for five minutes. Then, a solution prepared by
22 dissolving 300g of poly(vinylpyrrolidone) having a number average molecular
23 weight of 40,000 in 4,500g of water is sprayed from 2 nozzles onto the
24 powder. The coating conditions are monitored during the
poly(vinylpyrrolidone) solution spraying as follows: a total spray rate of
26 240 g/min from each nozzle, an inlet temperature of 45 C, an airflow of

27 1000 cfm. The coating process is computerized and automated in cycles.
28 Each cycle contained 30 seconds of solution spraying followed by two
29 seconds of drying and 10 seconds of filter bags with shaking to unglue
any possible powder deposits. At the end of the solution spraying period,


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9

1 the coated granulated particles are continued in the drying process for
2 25 minutes. The machine is turned off, and the coated granules are
3 removed from the coater. The coated granules are sized using a fluid air
mill.
4 The granulation is transferred to a mixer, mixed and lubricated with 50g of
magnesium stearate and mixed with 4g of butylated hydroxytoluene, to
6 provide the drug composition.

7 Next, a push-displacement composition is prepared as follows:
8 first, 7342g of poly(ethylene oxide) possessing a number average
9 molecular weight of 7 million, 2000g of sodium chloride, 200g of
hyd roxyp ropylmethylcel lu lose of 11,200 number average molecular weight,
11 100g of black ferric oxide are added to the Freund Flo-Coater's bowl.
12 The bowl is attached to the Flo-Coater and the granulation process is
started
13 to effect the process. The dry powders are air suspended and mixed for
14 six minutes. Then, a solution is prepared by dissolving 300g of
hydroxypropylmethylcellulose having a number average molecular weight of
16 11,200 in 4,500g of water is sprayed from 2 nozzles onto the air suspended
17 powder mix. The coating conditions were monitored during the
18 hydroxypropylmethylcellulose spraying of the solution. The conditions are
19 identical to those described in the above drug granulation process, except
for the drying cycle of less than 25 minutes. The granulated powders are
21 removed from the granulator and sized in a fluid air mill. The granulation
is
22 transferred to a blender, mixed and lubricated with 50g of magnesium
23 stearate and with 8 grams of butylated hydroxytoluene to yield,the push-
24 displacement composition.
Next, the drug composition and the push composition are compressed
26 into a bilayered core. First, 300 mg of the drug composition comprising
27 180 mg of verapamil hydrochloride is added to the punch and tamped, then
28 100 mg of the push displacement composition is added to the punch and the
29 layers pressed under a pressure of 2200 pounds into a 13/32 inch (1.032 cm)
diameter contacting, bilayered arrangement.


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WQ 97/37640 PCT/US97/044,_,
Next, the bilayered core is coated with a subcoat. The subcoat
2 comprises 95% hydroxyethylcellulose of 90,000 number average molecular
3 weight and 5% polyethylene glycol of 3350 average molecular weight. The
4 ingredients are dissolved in water to make a 5% solid solution. The subcoat
5 forming composition is sprayed onto and around the bilayer core in a 24 inch
6 Vector Hi-Coater. The dry subcoat weighed 79 mg.

7 Next, the hydroxyatkylcellulose, a hydroxyethylcellulose, a subcoated
8 bilayered cores are over coated with a semipermeable composition. The
9 overcoat membrane forming composition comprises 60% cellulose acetate
10 having an acetyl content of 39.8%, 35% hydroxypropylcellulose of 40,000
11 number average molecular weight and 5% polyethylene glycol of 3350 avg.
12 molecular weight is dissolved in methylene chloride: methanol (90:10 wt:wt)
13 cosolvent to make a 4% solid solution. The semipermeable membrane
14 forming composition is sprayed onto and around the subcoated bilayer core.
The semipermeable membrane, after drying weighed 43 mg.

16 Next, two 27 mil (0.686 mm) exit passageways are drilled through the
17 outer semipermeable membrane and the inner subcoat to connect the drug
18 layer with the exterior of the dosage form. The residual solvents are
removed
19 by drying for 96 hours at 50 C and 50% humidity. Finally, the dosage forms
are dried for 2 hours at 50 C to remove any excess moisture.

21 The dosage form manufactured by this procedure comprises a drug
22 composition with a weight of 300 mg, consisting of 180 mg of verapamil
23 hydrochloride, 91.41 mg of poly (ethylene oxide) of 300,000 molecular
weight,
24 12 mg of poly(vinylpyrrolidone) of 40,000 molecular weight, 15 mg of sodium
chloride, 0.12 mg of butylated hydroxy toluene and 1.5 mg of magnesium
26 stearate. A push-displacement composition that weighs 100 mg consisting of
27 73.5 mg of poly(ethylene oxide) of 7,000,000 molecular weight 20 mg of
28 sodium chloride, 5 mg of hydroxypropylmethylcelIulose of 11,200 molecular
29 weight, 0.92 mg of black ferric oxide, 0.08 mg of butylated hydroxytolune
and
0.5 mg of magnesium stearate. The dosage form subcoat weighed 78.8 mg


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x..,.97/37640 PCT/US97/04495
11
1 consisting of 74.86 mg of hydroxyethylcellulose of 90,000 molecular weight
2 and 3.94 mg of polyethylene glycol of 3350 molecular weight. The outer wall
3 weighed 42.6 mg consisting of 25.56 mg of cellulose acetate of 39.8% acetyl
4 content, 14.90 mg of hydroxypropylcellulose of 40,000 molecular weight, and
2.13 mg of polyethylene glycol of 3350 molecular weight. This dosage form
6 had a (dm/dt)t mean release rate of 18.6 mg/hr between the fourth and
7 ninth hour.

a The delivery pattern for the dosage form prepared by this example is
9 illustrated in figure 1. In figure 1, the nonuniform variability release
rate is
seen over the steady portion illustrated by the line starting at zero and
11 extended to the right of the figure. The release rate variation is for a
drug
12 having a 1 to 900 micron particle size released in the presence of a
13 hydrophilic polymer having greater than 25% particles larger then 250
micron.
14 The solid line depicts the % deviation from the total mean release rate.
The mean release rate for a given dosage form is expressed by the number
16 along the line starting at zero. In the figure No. 1 the erratic behavior
is
17 seen because the dosage form lacks uniform particles of a limited range.
18 The erratic behavior is characterized by a substantial deviation of
individual
19 system from the mean (dosage form) steady state release rate performance.
This erratic behavior phenomena is attributed to the inability of the
hydrophilic
21 polymer, the polyethylene oxide), to carry and suspend large drug
22 particles,(the verapamil hydrochloride), the difference in the hydration
time
23 between the large and small drug particles, and the larger hydrophilic
polymer
24 particles greater than 250 micron, which significantly changes the
hydration
and the drug suspending properties of the drug compositional layer that
26 resulted into a large percent negative deviation in the (dm/dt); from the
27 (dm/dt)t. The expression (dm/dt)t denotes the total mean release rate for
all
28 dosage forms in the zero portion, (dm/dt); denotes the mean release rate of
29 an individual dosage form in 4 to 9 hours, and (% dev); denotes the percent


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WO 97/37640 PCT/US97/0449:7,
12
deviation in an individual dosage form mean release rate, (4 to 9 hours) from
2 the total mean release rate. The figure reports results obtained from the
3 following equation:
4

(% dev) = m/ ; - (dm/dt)
6 (dm/dt)t
7

8 EXAMPLE 6
9

A dosage form for the delivery of a drug orally to a human is prepared
>> as follows: first 6000g of verapamil hydrochloride having a particle size
of
12 less than 150 micron, 3047g of polyethylene oxide) possessing a number
13 average molecular weight of 300,000 with 25% particles larger than
14 250 micron, 500g of sodium chloride, 100g of poly(vinylpyrrolidone) having
a number average molecular weight of 40,000 are added to the bowl of a fluid
16 bed granulator. The granulation is carried out for 7 to 10 minutes. Next,
the
17 dry powders are air suspended and mixed for five minutes. Then, a solution
18 is prepared by dissolving 300g of poly(vinylpyrrolidone) of 40,000 number
19 average weight in 4,500g of distilled water is sprayed from 2 nozzles onto
the
dry powder. The coating conditions are monitored during spraying as follows:
21 a total spray rate of 240 g/min from each nozzle, an inlet temperature of
45 C
22 and a process airflow of 1000 cfm. The coated process is automated in
23 cycles. Each cycle consist of 30 seconds of solution spraying followed by
24 two seconds of drying and 10 seconds of filter bags shaking to unglue and
possible powder deposits. At the end of the solution spraying time, the
26 coated granulated particles are continued with the drying process for
27 25 minutes. The machine is turned off, and the coated granules were
28 removed from the coater. The coated granules are sized using a fluid air
mill,
29 the granulation is transferred to a mixer, mixed and lubricated with 50
grams
of magnesium stearate and mixed with 4g of butylated hydroxytoluene to
31 provide the drug composition used for forming a layer in the bilayer core.


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\.=97/37640 PCT/CS97/04495
13
1 Next, a push composition is prepared as follows: first, 7342g of
2 poly(ethylene oxide) of 7,000,000 number average molecular weight, 2000g
3 of sodium chloride, 200g of hydroxypropylmethylcellulose of 11,200 number
4 average molecular weight, and 100 grams of black ferric oxide are added to
the bowl of a fluid bed granulator. The granulation process is started, and
the
6 dry powders are air suspended and mixed for 6 minutes. Then, a solution is
7 prepared by dissolving 300g of hydroxypropylmethylcellu lose possessing a
8 11,200 number average molecular weight in 4,500g of water that is sprayed
9 onto the air suspended powder mix. The coating conditions are monitored
during the spraying and the physical conditions are identical as described
>> for the above drug granulation, except that the drying cycle was less than
12 25 minutes. The granulated powders are removed from the granulator.
13 The granules are sized in a fluid air mill, then transferred to a blender
and
14 lubricated while mixing with 50g of magnesium stearate and 8g of butylated
hydroxytoluene to yield the push composition.
16 Next, the drug composition and the push composition are pressed into
17 a bilayered core, with the layers in contacting arrangement. First, 400 mg
of
18 the drug composition comprising 240 mg of verapamil hydrochloride is added
19 to a tablet punch and tamped, then 135 mg of the push composition is added
to the punch and the layers are pressed under a pressure head of 2300
21 pound in a 7/16 inch (1.11 cm) diameter contacting, bilayered arrangement.
22 The bilayered-core tablets are coated with a subcoat. The subcoat comprises
23 95% hyd roxya lkylcel I u lose, a (hyd roxyethylcel I u lose) of 90,000
molecular
24 weight and 5% polyethylene glycol of 3350 molecular weight, dissolved in
water to provide a 5% solid solution. The subcoat forming composition is
26 sprayed onto the around the bilayered core in a coater. The dry subcoat
27 weighed 93 mg.


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WO, 97/37640 PCT/i'S97/044y_,
14
1 Next, an outer coat is applied to the dosage form. The subcoated
2 bilayered-core tablets are coated with a semipermeable-membrane wall.
3 The membrane forming composition comprises 60% cellulose acetate having
4 a 39.8% acetyl content, 35% hydroxypropylcellulose of 40,000 molecular
weight and 5% polyethylene glycol of 3350 molecular weight. The wall
6 forming composition is dissolved in methylene chloride:methanol (90:10
wt:wt)
7 cosolvent to make a 4% solid solution. The semipermeable-membrane wall
8 forming composition is sprayed onto and around the subcoated bilayer core
9 in a coater to provide a two-coated dosage form. The semipermeable
membrane dry weighed 51 mg.
11 Next, two 27 mil (0.686 mm) exit passageways are drilled through the
12 outer and inner coats to connect the drug layer with the exterior of the
dosage
13 form. The residual solvents are removed by drying for 96 hours at 50 C and
14 50% humidity. Then, the osmotic dosage forms are dried for 2 hours at 50 C
to remove excess moisture.
16 The dosage form manufactured by this procedure comprises a drug
17 composition with a weight of 400 mg, consisting of 240 mg of verapamil
18 hydrochloride, 121.88 mg of polyethylene oxide of 300,000 molecular weight,
19 16 mg of poly(vinylpyrrolidone) of 40,000 molecular weight, 20 mg of sodium
chloride, 2 mg of magnesium stearate and 0.16 mg of butylated
21 hydroxytoluene. The push composition of the dosage form weighed 135 mg
22 and consists of 99.23 mg of poly(alkylene oxide), polyethylene oxide) of
23 7,000,000 molecular weight, 27 mg of sodium chloride, 6.75 mg of
24 hydroxypropylmethylcellulose of 11,200 molecular weight, 1.24 mg of
ferric oxide, 0.675 mg magnesium stearate, and 0.108 mg of butylated
26 hydroxytoluene. The inner subcoat weighed 93.1 mg and consists of
27 88.45 mg of the hydroalkylcellulose, hydroxyethylcellulose of 90,000
28 molecular weight and 46.55 mg of polyethylene glycol of 3350 molecular
29 weight. The outer coat weighed 51.1 mg and consists of 30.66 mg of
cellulose acetate of 39.8% acetyl content, 17.89 mg of hydroxypropylcellulose


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= ~. 0 97/37640 PCT/US97/04495
of 40,000 molecular weight and 2.57 mg of polyethylene glycol of 3350
2 molecular weight. The dosage form prepared by this example had a (dm/dt),
3 mean release rate of 27 mg/hr during hours 4 to 9.

4 The drug delivery pattern for the dosage form prepared by this
5 invention is seen in drawing figure 2. In figure 2, the nonuniform
variability is
6 depicted for the dosage form. The erratic release behavior is characterized
7 by a substantial and pronounced deviation of individual dosage forms from
8 the mean dosage form steady state rate performance. The figure denotes
9 that larger polymer particles of from 250 micron significantly change the
10 hydration and the drug carrying ability and suspension properties of the
11 drug composition. This results in a large percent negative deviation in the
12 expression (dm/dt); from the expression (dm/dt)t.

13

14 EXAMPLE 7

16 A dosage form for the delivery of a drug orally to the gastrointestinal
17 tract of a human in need of drug therapy is prepared as follows: first,
6000g
18 of verapamil hydrochloride having a particle size of 150 or smaller
microns,
19 3047g of polyethylene oxide) of 300,000 molecular weight and having a
particle of 250 or smaller microns, 500g of powdered sodium chloride, 100g of
21 poly(vinylpyrrolidone) having a 40,000 molecular weight are added to a
coater
22 and granulated in air for five minutes. Next, a solution is prepared by
23 dissolving 300g of poly(vinylpyrrolidone) of 40,000 molecular weight in
4,500g
24 of water and sprayed onto the powder. The spray rate is 240g/min at an
inlet
temperature of 45 C and an airflow of 1000 cfm. The spraying is effected in
26 two cycles consisting of 30 seconds of solution spraying followed by two
27 seconds of drying and 10 seconds of shaking to unglue powder deposits.
26 At the end of the solution spraying period, the coated granulated particles
are
29 dried for an additional 25 minutes. Then, the coated granules are sized in
a
fluid air mill. The granulation is transferred to a mixer, and lubricated with


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WO, 97/37640 PCTfUS97/0449,
16
1 50g of magnesium stearate and with 4g of butylated hydroxytoluene, to
2 yield the drug composition.

3 Next, a push displacement composition is prepared as follows:
4 first, 7342g of poly(ethylene oxide) of 7,000,000 molecular weight, 2000g
of sodium chloride, and 2000g of hydroxypropylmethylcellulose of 11,200
6 molecular weight, and 100g (grams) of black ferric oxide are added to the
7 bowl of a fluid bed granulator. The granulation is started and the powders
8 mixed for six minutes. Then, a solution is prepared by dissolving 300g of
9 hydroxypropylmethylcellulose of 11,200 molecular weight in water and
sprayed onto the air suspended particles. The coating process is as
11 described above. The granules are sized in a fluid air mill and transferred
to
12 a blender, and blended with 50g of magnesium stearate and 8g of butylated
13 hydroxytoluene, to yield the push-displacement composition.
14 Next, the drug composition and the push composition are compressed
into a bilayered tablet as follows: first, 400 mg of the drug composition
16 containing 240 mg of verapamil hydrochloride is added and tamped, then it
17 is overlayed with 135 mg of the push composition, and the two compositions
18 pressed under 2300 pounds into a 7/16 inch (1.11 cm) diameter contacting,
19 bilayered arrangement.
Next, the compressed bilayer tablets are coated with a subcoat
21 laminate. The subcoat comprises 95% hydroxyethylcellulose of 90,000
22 molecular weight and 5% polyethylene glycol of 3350 molecular weight
23 dissolved in distilled water to make a solid solution. The subcoat forming
24 composition is sprayed onto and around the bilayered tablet in a coater
to provide an encompassing laminate. The dry subcoat weighed 93 mg.
26 Next, the subcoat is overcoated with a semipermeable wall.
27 The semipermeable composition comprises 60% cellulose acetate having
26 an acetyl content of 39.8%, 35% hydroxypropylcellulose of 40,000 molecular
29 weight and 5% polyethylene glycol of 3350 average molecular weight.


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YO 97/37640 PCT/CS97/04495
17
1 The wall-forming composition is dissolved in a methylene-chloride: methanol
2 (90:10 wt:wt) cosolvent to make a 4% solid solution. The semipermeable
3 overcoat is sprayed onto and around to encase the subcoat. The
4 semipermeable wall weighed 51 mg.

s Next, two 27 mil (0.686 mm) exit passageway are drilled through the
6 dual oats to connect the drug layer with the exterior of the dosage form.
7 The residual solvents are removed by drying for 96 hours at 50 C and
8 50% humidity. Next, the osmotic, fluid imbibing dosage forms are dried
9 for 2 hours at 50 C to remove excess moisture.

The dosage form prepared by this example embraces the same
11 composition as the example immediately above, except for the controlled
12 drug particle size and the controlled hydrophilic polymer particle size in
the
13 drug composition. This double particle control produces substantially
uniform
14 dose dispensing, substantially-free of a wide variation in the dose
dispensing
pattern. Accompanying figure 3 depicts the drug delivery pattern for this
16 example. The figure depicts a release rate of (dm/dt)t equal to 27.9 mg/hr
17 during hours 4 to 9. The figure illustrates that a nonuniform variability
is not
18 observed for the dosage form provided by this example.

19

EXAMPLE 8
21

22 - A dosage form prepared according to Example 8 wherein the drug in
23 the dosage form is a calcium channel blocking drug selected from the group
24 consisting of isradipine, nilvadipine, flunarizine, nimodipine, diltiazem,
nicardipine, nitredipine, nisoldipine, filodipine, amlodipine, cinnarizine,
26 and fendiline.


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WQ 97/37640 I'CT/IIS97/0449n
18
EXAMPLE 9
2

3 The procedure described in the above is repeated in this example,
4 with the processing conditions as previously set forth, except that, in this
example the drug is an angiotensin converting enzyme inhibitor selected
6 from the group consisting of alacipril, benazepril, cialzepril, captropril,
7 delapril, enalapril, fosinopril, lisinopril, moveltypril, perindopril,
quinapril,
8 ramipril, spirapril, and zofenopril.

9

EXAMPLE 10
11

12 The procedures of the above examples are followed in this example
13 with the addition of the drug and is protected against oxidative attack and
14 oxidation by adding to the processing drug composition 0.05 ng to 7 mg of
an
antioxidant selected from the group consisting of d-alpha tocopherol, di-alpha
16 tocopherol, d-alpha tocopherol acetate, d-alpha tocopherol acid succinate,
17 dl-alpha tocopherol acid succinate, dl-alpha tocopherol palmitate, ascorbic
18 acid, ascorbyl oleate, ascorbyl palmitate, butylated hydroxyanisole,
butylated
19 hydroxytoluene, sodium ascorbate, calcium ascorbate, and propyl gallate
stabilizers.
21

'-= EXAMPLE 11
23

24 The procedures of the above examples are followed in this example
with an addition to the drug composition comprising 0.05 ng to 7 mg of an
26 antioxidant stabilizer and 0.05 ng to 7.5 mg of a lubricant selected from
the
27 group consisting of magnesium stearate, calcium stearate, magnesium
28 oleate, magnesium palmitate, corn starch, potato starch, bentonite, citrus
29 pulp, and stearic acid; and, with all the ingredients in the drug
composition
when expressed in weight percent equal to 100 wt% weight percent.


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97/37640 PCT/1; S97/0449;
19

EXAMPLE 12
z

3 The procedures of the above examples are followed in this example
4 with an addition to the drug composition of means protection the drug
against
daylight and ultraviolet light; wherein, the addition comprising adding to the
6 drug composition 0.01 mg to 10 mg of surface-active agent selected from
7 anionic, cationic, amphoteric and nonionic surfactants including dialkyl
a sodium sulfosuccinate, polyoxyethylene glycerol, polyoxyethylene stearyl
9 ether, propoxy-ethoxy copolymer, polyoxyethylene fatty alcohol ester,
polyoxyethylene fatty acid ester, ethoxylated hydrogenated castor oil, and
11 butoxylated hydrogenated castor oil; and adding to the drug composition
12 0.01 mg to 10 mg of riboflavin to stabilize the drug against light.

13

14 ADDITIONAL DISCLOSURE OF THE INVENTION
16 In the specification and in the accompanying claims, the term
17 beneficial agent also includes drugs. The term drug includes any
18 physiologically or pharmacologically active substance that produces a local
19 or a systemic effect, in animals, including warm-blooded mammals, humans
and primates; avians, household, sport, and farm animals; laboratory animals;
21 fishes; reptiles; and zoo animals. The term "physiologically" as used
herein,
22 generically denotes the administration of a drug to produce generally
normal
23 drug levels and functions. The term "pharmacologically" denotes generally
24 variations in response to the amount of drug administered to a host. The
drug
can be in various forms such as unchanged molecules, molecular complexes,
26 pharmacologically acceptable salts such as hydrochloride, hydrobromide,
27 sulfate, laurate, palmitate, phosphate, nitrite, nitrate, borate, acetate,
maleate,
28 tartiate, oleate, salicylate, and the like. For acidic drugs, salts of
metals,
29 amines, or organic cations, for example quarternary ammonium can be used.
Derivatives of drugs, such as bases, ester and amide can be used. A drug


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WO 97/37640 PCT/US97/0449-,
1 that is water insoluble can be used in a form that is water soluble
derivative
2 ' thereof, or as a base derivative thereof, which in either instance or in
its
3 delivery by the osmotic system, is converted by enzymes, hydrolyzed by the
4 body pH, or by other metabolic processes to the original therapeutically
active
5 form. The amount of drug in a dosage form, that is, in the drug composition
is
6 25 ng to 750 mg. The dosage form comprising the drug can be administered,
7 once, twice, or thrice daily.

8 The active drug that can be delivered includes inorganic and organic
9 compounds without limitation, including drugs that act on the peripheral
10 nerves, adrenergic receptors, cholinergic receptors, nervous system,
skeletal
>> muscles, cardiovascular system, smooth muscles, blood circulatory system,
12 synoptic sites, neuroeffector junctional sites, endocrine system, hormone
13 systems, immunological system, organ systems, reproductive system,
14 skeletal system, autocoid systems, alimentary and execretory systems,
15 inhibitory of autocoids and histamine systems, and physiological systems.
16 The active drug that can be delivered for acting on these animal systems
17 includes depressants, beta-blockers, hypnotics, sedatives, psychic
18 energizers, tranquilizers, anti-convulsants, muscle relaxants, steroids,
19 antiparkinson agents, analgesics, anti-inflammatories, polypeptides, local
20 anesthetics, muscle contractants, anti-microbials, antimalarials, hormonal
21 agents, contraceptives, sympathomimetics, diuretics, anti-parasitics,
22 neoplastics, hypoglycemics, ophthalmics, electrolytes, diagnostic agents,
23 cardiovascular drugs, calcium channel blockers, angio-tensin-converting
24 enzyme inhibitors, and the like.
Exemplary of drugs that can be delivered from the dosage form of
26 this invention include a drug selected from the group consisting of
amifostine,
27 prochlorperazine edisylate, ferrous sulfate, aminocaprioc acid, potassium
28 chloride, mecamylamine hydrochloride, procainamide hydrochloride,
29 amphetamine sulfate, benzphetamine hydrochloride, isoproternal sulfate,
methamphetamine hydrochloride, phenmetrazine hydrochloride, bethanechol


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~. 1737640 PCT/US97/04495
21
1 chloride, methacholine chloride, pilocarpine hydrochloride, antropine
sulfate,
2 methascopolamine bromide, isopropamide iodide, tridihexethyl chloride,
3 phenformin hydrochloride, methylphenidate hydrochloride, oxprenolol
4 hydrochloride, metroprolol tartrate, cimetidine hydrochloride, diphenidol,
meclizine hydrochloride, prochlorperazine maleate, phenoxybenzamine,
6 thiethylperzine, maleate, anisindone, diphenadione erythrityl teranitrate,
7 dizozin, isofurophate, reserpine, acetazolamide, methazolamide,
8 bendroflumenthiazide, chlorpropamide, tolazamide, chlormadinone acetate,
9 phenaglycodol, allopurinol, aluminum aspirin, methotrexate, acetyl
sulfisoxazle, erythromycin, progestins, estrogenic progrestational,
11 corticosteroids, hydrocortisone acetate, cortisone acetate, triamcinolone,
12 methyltesterone, 173-estradiol, ethinyl estradiol, ethinyl estradiol 3-
methyl
13 ether, prednisolone, 17-hydroxyprogesterone acetate, 19-nor-progesterone,
14 norgestrel, norethindone, norethiderone, progesterone, norgestrone,
orethynodrei, aspirin, indomethacin, aproxen, fenoprofen, sulidac, diclofenac,
16 indoprofen, nitroglycerin, propranolol, metroprolol, valiproate,
oxyprenolol,
17 timolol, atenolol, alpreholol, cimetidine, clonidine, imipramine, levodopa,
18 chloropropmazine, resperine, methyldopa, dihydroxyphenyllalanine,
19 pivaloyloxyethyl ester of s-methyldopa hydrochloride, theophylline, calcium
gluconate ferrous lactate, ketoprofen, ibuprofen, cephalexin, erythromycin,
21 haloperiodol, zomepirac, vincamine, diazepam, phenoxybenzamine,
22 3-blocking agents; calcium-channel blocking drugs such as nifedipine,
23 diltiazem, isradipine, nilvadipine verapamil, fiunarizine, nimodipine,
felodipine,
24 amlodipine, cinnarizine and fendiline; angiotensin converting enzyme
inhibitors selected from the group consisting of angiotensin converting
26 enzyme inhibitors that are essentially free of sulfur, angiotensin
converting
27 enzyme inhibitors containing a sulfhydryl group, angiotensin converting
28 enzyme inhibitors containing a linear sulfide, angiotensin converting
enzyme
29 inhibitors containing a cyclic sulfide angiotensin converting enzyme
inhibitors
containing a methylsulfonyl group and angiotensin enzyme inhibitors


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WO 97/37640 PCTIUS97/0449.
22
1 represented by a member selected from the group consisting of ramipril,
2 fosinopril, altiopril, benazepril, libenzapril, alacepril, citazapril,
cilazaprilate,
3 perindopril, zofenopril, enalapril, lisinopril, imidapril, spirapril,
rentrapril,
4 captopril, delapril, alindapril, indolapril, and quinapril; propranolol,
naproxen,
phenylpropanolamine, glipizide, venlafaxine, and beneficial drugs known to
6 the dispensing arts in Pharmaceutical Sciences, 1990, edited by Remington
7 18th Edition published by Mack Publishing Co., Easton, PA; Physicians' Desk
s Reference, 50th Edition, (1996) published by Medical Economics Co.,
9 Montvale, NJ, and, USP Dictionary, 1995, published by the United States
Pharmacopeial Convention, Inc., Rockville, Maryland.
11 The dosage form of the invention is provided with at least one exit
12 means. The exit means cooperates with the drug core for the uniform and
13 substantially nonvarying drug-dose release from the dosage form. The exit
14 means can be provided during manufacture of the dosage form, or the exit
means can be provided during drug delivery by the dosage form in fluid
16 environment of use. The expression exit means, as used for the purpose of
17 this invention, included a member selected from the group consisting of
18 passageway, aperture, orifice, bore, pore, micropore, porous element
19 through which a drug can be pumped, diffuse, travel, or migrate, a hollow
fiber, capillary tube, porous insert, porous overlay, microporous member,
21 and porous composition. The expression includes also a compound or
22 polymer that erodes, dissolves or is leached from the outer coat or wall,
23 or from the inner coat to form at least one exit, or a multiplicity of
exits.
24 The compound or polymer includes an erodible poly (glycolic) acid or
poly (lactic) acid in the outer or inner coats, a gelatinous filament,
26 a water-removable poly (vinyl alcohol), a leachable compound such as
27 a fluid removable pore-former selected from the group consisting of an
28 inorganic, organic, acid, salt, oxide, and carbohydrate. An exit or a
plurality
29 of exits can be formed by leaching a member selected from the group
consisting of sorbitol, lactose, fructose, glucose, mannose, galactose,
talose,


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_,. 97/37640 PCT/L' S97/04495
23

1 sodium chloride, potassium chloride, sodium citrate, and mannitol; to
provide
2 an uniform-release dimensioned pore-exit means. The exit means can have
3 any shape such as round, triangular, square, elliptical and the like for the
4 uniform-metered dose release of a drug from the dosage form. The dosage
form can be constructed with one or more than one exits in spaced apart
6 relation or one or more than one surface of the dosage form. The exit means
7 can be performed by drilling including mechanical and laser drilling through
a the outer, or inner or through both coats. Exits and equipment for forming
9 exits are disclosed in U.S. Pat. Nos. 3,845,770 and 3,916,899 by Theeuwes
and Higuchi; in U.S. Pat. Nos. 4,063,064 by Saunders, et al; and in U.S. Pat.
11 No. 4,088,864 by Theeuwes, et al. Exit means comprising dimension, sized,
12 shaped and adapted as a releasing-pore formed by aqueous leaching to
13 provide a drug releasing pore are disclosed in U.S. Pat. Nos. 4,200,098
14 and 4,285,987 by Ayer and Theeuwes.
The particles used for the purpose of this invention are produced by
16 comminution that produces the size of the drug and the size of the
17 accompanying hydrophilic polymer used according to the mode and the
18 manner of the invention. The means for producing particles include spray
19 drying, sieving, Iyophilization, sieving, crushing, grinding, jet milling
micronizing and chopping to produce the intended micron particle size.
21 The process can be performed by size reduction equipment such as
22 micropulverizer mill, fluid energy grinding mill, grinding mill, roller
mill,
23 hammer mill, attrition mill, chaser mill, ball mill, vibrating bail mill,
impact
24 pulverizer mill, centrifugal pulverizer, coarse crusher and fine crusher.
The size of the particle can be ascertained by screening including grizzly
26 screen, flat screen, vibrating screen, revolving screen, shaking screen,
27 oscillating screen and reciprocating screen. The processes and the
28 equipment for preparing particles are disclosed in Pharmaceutical Sciences
29 by Remington, 17th Ed., pg. 1585-1594, (1985); Chemical Engineers!
Handbook, by Perry, Sixth Edition, pg. 21-13 to 21-19 (1984); Journal of


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WO 97/37640 PCT/US97/044..
24
1 Pharmaceutical Sciences, by Parrot, Vol. 61, No., 6, pg. 813 to 829 (1974)1-
2 and Chemical Engineer, by Hixon, pg. 94 to 103, (1990).

3 In accordance with the practice of this invention, it has now been found
4 the dosage can be provided with a semipermeable wall, also identified for
the purpose of this invention as an outercoat. The semipermeable wall is
6 permeable to the passage of an external fluid such as water and biological
7 fluids, an it is substantially impermeable to the passage of a beneficial
agent,
8 as osmogent, an osmopolymer, and the like. The selectively semipermeable
s compositions used for forming the wall are essentially non-erodible and they
are insoluble in biological fluids during the life of the dosage form.
11 Representative polymers for forming the wall comprise semipermeable
12 homopolymers, semipermeable copolymers, and the like. In one presently
13 preferred embodiment, the compositions comprise cellulose esters, cellulose
14 ethers, and cellulose ester-ethers. The cellulosic polymers have a degree
of substitution, D.S. of their anhydroglucose unit from greater than 0 up
16 to 3 inclusive. By degree of substitution is meant the average number
17 of hydroxyl groups originally present on the anhydroglucose unit that
18 are replaced by a substituting group, or converted into another group.
19 The anhydroglucose unit can be partially or completely substituted with
groups such as acyl, alkanoyl, alkenoyl, aroyl, alkyl, alkoxy, halogen,
21 carboalkyl, alkylcarbamate, alkylcarbonate, alkylsulfonate, alkysulfamate,
22 semipermeable polymer forming groups, and the like.
23 The semipermeable compositions typically include a member selected
24 from the group consisting of cellulose acylate, cellulose diacylate,
cellulose
triacylate, cellulose triacetate, cellulose acetate, cellulose diacetate,
cellulose
26 triacetate, mono-, di- and tri-cellulose alkanylates, mono-, di-, and tri-
27 alkenylates, mono-, di-, and tri-aroylates, and the like. Exemplary
polymers
28 include cellulose acetate have a D.S. of 1.8 to 2.3 and an acetyl content
of
29 32 to 39.9%; cellulose diacetate having a D.S. of 1 to 2 and an acetyl
content
of 21 to 35%, cellulose triacetete having a D.S. of 2 to 3 and an acetyl
content


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97/37640 PCT/US97/04495

1 of 34 to 44.8%, and the like. More specific cellulosic polymers include
2 cellulose propionate having a D.S. of 1.8 and a propionyl content of 38.5%;
3 cellulose acetate propionate having an acetyl content of 1.5 to 7% and an
4 acetyl content of 39 to 42%; cellulose acetate propionate having an acetyl
5 content of 2.5 to 3%, an average propionyl content of 39.2 to 45%, and a
6 hydroxyl content of 2.8 to 5.4%; cellulose acetate butyrate having a D.S.
7 of 1.8, an acetyl content of 13 to 15%, and a butyryl content of 34 to 39%;
a cellulose acetate butyrate having an acetyl content of 2 to 29%, a butyryl
9 content of 17 to 53%, and a hydroxyl content of 0.5 to 4.7%; cellulose
10 triacylates having a D.S. of 2.6 to 3 such as cellulose trivalerate,
cellulose
11 trilamate, cellulose tripalmitate, cellulose trioctanote, and cellulose
12 tripropionate; cellulose diesters having a D.S. of 2.2 to 2.6 such as
cellulose
13 disuccinate, cellulose dipalmitate, cellulose dioctanoate, cellulose
dicarpylate,
14 and the like; mixed cellulose esters such as cellulose acetate valerate,
15 cellulose acetate succinate, cellulose propionate succinate, cellulose
acetate
16 octanoate, cellulose valerate palmitate, cellulose acetate heptonate, and
the
17 like. Semipermeable polymers are known in US Pat. No. 4,077,407 and they
18 can be synthesized by procedures described in Encyclopedia of Polymer
19 Science and Technology, Vol. 3, pages 325 to 354, 1964, published by
20 Interscience Publishers, Inc., New York.

21 Additional semipermeable polymers for forming the outer wall comprise
22 cellulose acetaldehyde dimethyl acetate; cellulose acetate ethylcarbamate;
23 cellulose acetate methyl carbamate; cellulose dimethylaminoacetate;
24 semipermeable polyamide; semipermeable polyurethanes; semipermeable
25 sulfonated polystyrenes; cross-linked selectively semipermeable polymers
26 formed by the coprecipitation of a polyanion and a polyication as disclosed
27 in U.S. Pat. Nos. 3,173,876; 3,276,586; 3,541,005; 3,541,006; and
3,546,142;
28 semipermeable polymers as disclosed by Loeb et al in U.S. Pat.
29 No. 3,133,132; semipermeable polystyrene derivatives; semipermeable


CA 02586473 2007-04-30

v0 97/37640 PC'T/t'S97IO44`,_
26

1 poly (sodium styrenesulfonate); semipermeable poly
2 (vinylbenzyltremethylammonium chloride); semipermeable polymers,
3 exhibiting a fluid permeability of 10-5 to 10-2 (cc. mil/cm hr.atm)
expressed
a as per atmosphere of hydrostatic or osmotic pressure differences across a
semipermeable wall. The polymers are known to the art in U.S. Pat.
6 Nos. 3,845,770; 3,916,899; and 4,160,020; and in Handbook of Common
7 Polymers, by Scott, J.R., and Roff, W.J., 1971, published by CRC Press,
8 Cleveland, Ohio.

9 The subcoat of the invention is in contacting position with the
inner surface of the semipermeable wall, which outer semipermeable
11 wall surrounds and encases the inner subcoat. The inner subcoat is
12 0.01 mm to 3 mm thick and it comprises a member selected from
13 group consisting of hydroxyalkyl, hydroxyethylceliulose,
14 hydroxyisopropylcelluose, hydroxybutylcellulose, and
hydroxyphenylcellulose.
The hydroxyalkyl cellulose comprises a 9,500 to 1,250,000 number average
16 molecular weight.
17 The drug composition comprised a hydrophilic polymer for providing
18 in the drug composition a hydrophilic polymer particle that contributes to
the
19 uniform and nonvarying drug delivery pattern. Representatives of these
polymers comprise a member selected from the group consisting of a poly
21 (alkylene oxide) of 100,000 to 750,000 number average molecular weight
22 including poly (ethylene oxide), poly (methylene oxide), poly (butylene
oxide),
23 and poly (hexylene oxide); and a poly (carboxymethylcellulose) of 40,000 to
24 400,000 number average molecular weight represented by poly (alkali
carboxymethylcellulose), poly (sodium carboxymethylcelluose), poly
26 (potassium carboxymethylcellulose), and poly (lithium
27 carboxymethylcellulose). The drug composition can comprise a
28 hydroxypropylalkylcellulose of 9,200 to 125,000 number average
29 molecular weight for enhancing the delivery properties of the dosage


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V* 0,97/37640 PCT/US97/04495
27
1 form as represented by hydroxypropylethylcellulose,
2 hydroxypropylmethylcellulose, hydroxypropylbutylcellulose, and
3 hydroxypropylpentylcellulose: and a poly (vinylpyrrolidone) of
4 7,000 to 75,000 number average molecular weight for enhancing
the flow properties of the dosage form.

6 The push-displacement composition in contacting layered arrangement
7 comprised a polymer that imbibes an aqueous or biological fluid and swells
to
8 push the drug composition through the exit means from the dosage form.
9 Representative of fluid-imbibing displacement polymers comprise a member
selected from the group consisting of a poly (alkylene oxide) of 1,000,000 to
11 15,000,000 number average molecular weight as represented by poly
12 (ethylene oxide) and a poly (alkali carboxymethylcelIulose) of 500,000 to
13 3,500,000 number average molecular weight wherein the alkali is sodium,
14 potassium or lithium. Examples of further polymers for formulation, the
push-
displacement composition comprise osmopolymers comprise polymers that
16 form hydrogels such as Carbopol acidic carboxypolymer, a polymer of
17 acrylic and cross-linked with a polyallyl sucrose, also known as
18 carboxypolymethylene and carboxyvinyl polymer having a molecular weight
19 of 250,000 to 4,000,000; Cyanamer polyacrylamides; cross-linked water
swellable indenemaleic anhydride polymers; Good-rite polyacrylic acid
21 having a molecular weight of 80,000 to 200,000; Aqua-Keeps acrylate
22 polymer polysaccharides composed of condensed glucose units such as
23 diester cross-linked polygluran; and the like. Representative polymers that
24 form hydrogels are known to the prior art in U.S. Pat. No. 3,865,108 issued
to Hartop; U.S. Pat No. 4,002,173 issued to Manning; U.S. Pat. No.
26 4,207,893 issued to Michaels; and in Handbook of Common Polymers,
27 by Scott and Roff, published by the Chemical Rubber Co., Cleveland, Ohio.
28 The osmagent, also known as osmotic solute and as osmotically
29 effective agent, that exhibits an osmotic pressure gradient across the
outer
wall and subcoat comprises a member selected from the group consisting of


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WO 97/37640 PCT/US97/0419-j
28
sodium chloride, potassium chloride, lithium chloride, magnesium sulfate,
2 magnesium chloride, potassium sulfate, sodium sulfate, lithium sulfate,
3 potassium acid phosphate, mannitol, urea, inosital, magnesium succinate,
a tartaric acid raffinore, sucrose glucose, lactose, sorbitol, inorganic
salts,
organic salts and carbohydrates.

6 Exemplary solvents suitable for manufacturing the hydroactivated layer
7 and the wall comprise inert inorganic solvents that do not adversely harm
the
8 materials, the capsule, and the final laminated wall hydro-activated layer.
9 The solvents broadly include members selected from the group consisting of
aqueous solvents, alcohols, ketones, esters, ethers, aliphatic hydrocarbons,
11 halogenated solvents, cycloaliphatic, aromatics, heterocyclic solvents and
12 mixtures thereof. Typical solvents include acetone, diacetone alcohol,
13 methanol, ethanol, isopropyl alcohol, butyl alcohol, methyl acetate, ethyl
14 acetate, isopropyl acetate, n-butyl acetate, methyl isobutyl ketone, methyl
propyl ketone, n-hexane, n-heptane, ethylene glycol monoethyl ether,
16 ethylene glycol monothyl acetate, methylene dichloride, ethylene
dichloride,
17 propylene dichloride, carbon tetrachloride nitroethane, nitropropane
18 tetrachloroethane, ethyl ether, isopropyl ether, cyclohexane. cyclooctane,
19 benzene, toluene, naphtha, 1,4-dioxane, tetrahydrofuran, diglyme, water,
aqueous solvents containing inorganic salts such as sodium chloride,
21 calcium chloride, and the like, and mixture thereof such as acetone and
22 water, acetone and methanol, acetone and ethyl alcohol, methylene
23 dichloride and methanol, and ethylene dichloride and methanol.
24 The semipermeable wall and the subcoat of the dosage form can
be formed in one technique using the air suspension procedure. This
26 procedure consists of suspending and tumbling the bilayer core in a current
27 of air, an inner subcoat composition and an outer semipermeable wall
forming
28 composition, until in either operation the subcoat and the outer wall coat
is
29 applied to the bilayer core. The air suspension procedure is well-suited
for
independently forming the wall of the dosage form. The air suspension


CA 02586473 2007-04-30

97/37640 PCT/1JS97/04495
29

1 procedure is described in U.S. Pat. No. 2,799,241; in J. Am. Pharm. Assoc.,
2 Vol. 48, pp. 451 to 459, (1959); and, ibid, Vol. 49, pp. 82 to 84, (1960).
3 The dosage form also can be coated with a Wurster air suspension coater,
4 using for example, methylene dichloride methanol as a cosolvent.
An Aeromatic air suspension coater can be used employing a cosolvent.
6 Other coating techniques, such as pan coating, can be used for providing
7 the dosage form. In the pan coating system, the subcoat on the wall forming
8 compositions are deposited by successive spraying of the respective
9 compensation on the bilayered core accompanied by tumbling in a rotating
pan. A pan coater is used because of its availability at commercial scale.
11 Other techniques can be used for coating the drug core. Finally, the wall
or
12 coated dosage form are dried in a forced air oven at 40 C. for a week, or
in
13 a temperature and humidity controlled oven for 24 hours at 40 C. and 50%
14 relative humidity to free the dosage form of solvent.
The dosage form of the invention is manufactured by standard
16 techniques. Fro example, in one manufacture, the beneficial drug and other
17 ingredients comprising the first layer facing the exit means are blended
and
18 pressed into a solid layer. The layer possesses dimensions that correspond
19 to the internal dimensions of the area the layer is to occupying the dosage
form and it also possesses dimensions corresponding to the second layer for
21 forming a contacting arrangement therewith. The drug and other ingredients
22 can be blended also with a solvent and mixed into a solid or semisolid form
by
23 conventional methods, such as ballmilling, calendering, stirring or
rollmilling,
24 and then pressed into a preselected shape. Next, a layer of osmopolymer
composition is placed in contact with the layer of drug in a like manner.
26 The layering of the drug formulation and the osmopolymer layer can be
27 fabricated by conventional two-layer press techniques. The two contacted
28 layers are first coated with a subcoat and an outer semipermeable wall.
29 The air suspensions and air tumbling procedures comprises in suspending


CA 02586473 2007-04-30

WO 97/37640 PCT/LS97/044
1 and tumbling the pressed, contacting first and second layers in a current of
2 air containing the delayed-forming composition until the first and second
3 layers are surrounded by the wall composition.

4 In another manufacture, the dosage form is manufactured by the wet
5 granulation technique. In the wet granulation technique, the drug and the
6 ingredients comprising the first layer or drug composition, are blended
using
7 an organic solvent, such as denature anhydrous ethanol, as the granulation
a fluid. The ingredients forming the first layer or drug composition are
9 individually passed through a preselected screen and then thoroughly
10 blended in a mixer. Next, other ingredients comprising the first layer can
11 be dissolved in a portion of the granulation fluid, the solvent described
above.
12 Then, the latter prepared wet blend is slowly added to the drug blend with
13 continual mixing in the blender. The granulating fluid is added until a wet
14 blend is produced, which wet mass blend is then forced through a
15 predetermined screen onto oven trays. The blend is dried for 18 to 24 hours
is at 24 C. to 35 C. in a forced air oven. The dried granules are then sized.

17 Next, magnesium stearate is added to the drug granulation, it is then put
18 into milling jars and mixed on a jar mill for 10 minutes. The composition
is
19 pressed into a layer, for example, in a Manesty press. The speed of the
20 press is set at 20 rpm and the maximum load set at 2 tons. The first layer
21 is pressed against the composition forming the second layer and the bilayer
22 tablets are fed to the Kilian dry Coata press and surrounded with the drug-

23 free coat, followed by the exterior wall solvent coating.
24 Another manufacturing process that can be used for providing
25 the compartment-forming composition comprises blending the powdered
26 ingredients in a fluid bed granulator. After the powdered ingredients
27 are dry blended in the granulator, a granulating fluid, for example,
28 poly(vinylpyrrolidone) in water, is sprayed onto the powders. The coated
29 powders are then dried in the granulator. This process granulates all the
30 ingredients present therein while adding the granulating fluid. After the


CA 02586473 2007-04-30

97/37640 PCTIL'S97/04495
31

1 granules are dried, a lubricant such as stearic acid or magnesium stearate
is
2 mixed into the granulation, using a V-blender. The granules are then pressed
3 in the manner described above.

4

METHOD OF PRACTICING THE INVENTION
6

7 The invention provides a process for the substantially uniform and
a substantially nonvarying rate of release of a drug from a dosage form,
herein
9 the dosage form comprises a composition, a dose of drug in the composition,
and a hydrophilic polymer in the composition, and wherein the process
11 comprises (1) formulating the composition with a drug possession, a
particle
12 size up to and including 150 microns, and (2) formulating the composition
13 with a hydrophilic polymer possessing a particle size up to and including
14 250 microns, hereby, through the copresence of (1) and (2) in the
composition, the drug is delivered as the substantially uniform and
16 nonvarying rate of release from the dosage form.
17 The invention provides also a process for substantially uniform
18 and substantially nonvarying rate of release of a drug from a dosage form,
19 wherein the dosage form comprises a composition, a dose of drug in the
composition, a hydrophilic polymer in the composition, and a composition
21 for displacing the drug composition from the dosage form, and wherein the
22 process comprises (1) formulating the composition with a drug possessing
23 a particle size up to and including 150 micron, (2) formulating the
24 composition with a hydrophilic polymer possessing a particle size up to
and including 150 microns, whereby through the copresence of (1) and
26 (2) in combination with the composition for displacing the drug composition
27 imbibing fluid, expanding and displacing the drug composition from the
28 dosage form. The drug is delivered at a substantially uniform and
nonvarying
29 rate of release over time.


CA 02586473 2007-04-30

WC) 97/37640 PCT/17S97/044:,
32
1 The invention comprises also a method for delivering a drug to a
2 patient, wherein the method comprises: (A) admitting orally into the patient
a
3 dosage form comprising: (1) a semipermeable wall that surrounds and forms
4 a compartment; (2) a drug composition in the compartment; (3) a dose of
drug particles up to 150 micron in the drug composition; (4) a hydrophilic
6 polymer of up to 250 micron in the drug composition; (5) an exit in the
7 semipermeable wall; (B) imbibing fluid through the semipermeable wall
8 into the drug composition whereby through the coaction of (2) and
9 (3) a dispensable drug composition is formed in the dosage form; and
(C) delivering the drug composition through the exit to a patient at a
11 substantially uniform and nonvarying dose over time.

12 The invention comprises further a method for providing a drug-free
13 interval by placing a subcoat in the dosage form in contact with the inside
14 surface of the semipermeable wall and surrounding the drug composition,
or surrounding both a drug composition and a push composition, which
16 drug-free interval is followed in 2 to 5 hours by a drug delivery period of
17 1 to 15 hours. The latter method is indicated for the treatment of
18 hypertension and angina as it provides a drug-free interval when a patient
19 is less active, thus, at rest or when asleep, and the inventive method then
provides drug during the rising and waking hours mainly during the time
21 when activity reaches a maximum during the daytime hours.
22 -The method of the invention pertains also to the management of
23 blood pressure, the management of the systemic physiology, and to the
24 management of chronotherapy, that is timetherapy by administering a
drug according to the mode and the manner of the invention.
26 The novel dosage form of this invention uses dual means for the
27 attainment of precise release rate of drugs that are difficult to deliver
in the
28 environment of use, while simultaneously maintaining the integrity and the
29 character of the system. While there has been described and pointed out


CA 02586473 2007-04-30

97/37640 PCTrt'. 597/0449;
33

features and advantages of the invention, as applied to the presently
2 preferred embodiments, those skilled in the dispensing art will appreciate
3 that various modifications, changes, additions, and omissions in the system
4 illustrated and described can be made without departing from the spirit of
the invention.

Representative Drawing
A single figure which represents the drawing illustrating the invention.
Administrative Status

For a clearer understanding of the status of the application/patent presented on this page, the site Disclaimer , as well as the definitions for Patent , Administrative Status , Maintenance Fee  and Payment History  should be consulted.

Administrative Status

Title Date
Forecasted Issue Date 2011-05-31
(22) Filed 1997-03-20
(41) Open to Public Inspection 1997-10-16
Examination Requested 2007-10-17
(45) Issued 2011-05-31
Expired 2017-03-20

Abandonment History

There is no abandonment history.

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Registration of a document - section 124 $100.00 2007-04-30
Registration of a document - section 124 $100.00 2007-04-30
Application Fee $400.00 2007-04-30
Maintenance Fee - Application - New Act 2 1999-03-22 $100.00 2007-04-30
Maintenance Fee - Application - New Act 3 2000-03-20 $100.00 2007-04-30
Maintenance Fee - Application - New Act 4 2001-03-20 $100.00 2007-04-30
Maintenance Fee - Application - New Act 5 2002-03-20 $200.00 2007-04-30
Maintenance Fee - Application - New Act 6 2003-03-20 $200.00 2007-04-30
Maintenance Fee - Application - New Act 7 2004-03-22 $200.00 2007-04-30
Maintenance Fee - Application - New Act 8 2005-03-21 $200.00 2007-04-30
Maintenance Fee - Application - New Act 9 2006-03-20 $200.00 2007-04-30
Maintenance Fee - Application - New Act 10 2007-03-20 $250.00 2007-04-30
Request for Examination $800.00 2007-10-17
Maintenance Fee - Application - New Act 11 2008-03-20 $250.00 2008-02-05
Maintenance Fee - Application - New Act 12 2009-03-20 $250.00 2009-02-06
Maintenance Fee - Application - New Act 13 2010-03-22 $250.00 2010-02-09
Maintenance Fee - Application - New Act 14 2011-03-21 $250.00 2011-02-04
Final Fee $300.00 2011-03-17
Maintenance Fee - Patent - New Act 15 2012-03-20 $450.00 2012-02-08
Maintenance Fee - Patent - New Act 16 2013-03-20 $450.00 2013-02-13
Maintenance Fee - Patent - New Act 17 2014-03-20 $450.00 2014-02-14
Maintenance Fee - Patent - New Act 18 2015-03-20 $450.00 2015-02-25
Maintenance Fee - Patent - New Act 19 2016-03-21 $450.00 2016-02-24
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
ALZA CORPORATION
Past Owners on Record
AYER, ATUL DEVDATT
HAMEL, LAWRENCE G.
LAM, ANDREW
MAGRUDER, JUDY A.
WONG, PATRICK S.-L.
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Abstract 2007-04-30 1 5
Description 2007-04-30 36 1,730
Claims 2007-04-30 4 125
Drawings 2007-04-30 3 31
Representative Drawing 2007-07-16 1 5
Cover Page 2007-07-25 1 29
Description 2010-03-22 36 1,747
Claims 2010-03-22 5 136
Claims 2009-06-25 4 122
Description 2009-06-25 36 1,730
Cover Page 2011-05-09 1 29
Prosecution-Amendment 2009-09-22 2 62
Correspondence 2007-05-25 1 36
Assignment 2007-04-30 2 92
Correspondence 2007-07-28 1 14
Prosecution-Amendment 2007-10-17 1 40
Prosecution-Amendment 2010-03-22 15 589
Prosecution-Amendment 2009-06-02 2 42
Prosecution-Amendment 2009-06-25 11 370
Correspondence 2011-03-17 2 59