GB2170104A - Coated pharmaceutical dosage forms - Google Patents

Coated pharmaceutical dosage forms Download PDF

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Publication number
GB2170104A
GB2170104A GB08601389A GB8601389A GB2170104A GB 2170104 A GB2170104 A GB 2170104A GB 08601389 A GB08601389 A GB 08601389A GB 8601389 A GB8601389 A GB 8601389A GB 2170104 A GB2170104 A GB 2170104A
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GB
United Kingdom
Prior art keywords
coating
process according
overcoat
dosage forms
coated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
GB08601389A
Other versions
GB8601389D0 (en
Inventor
Isaac Ghebre-Sellassie
Robert H Gordon
Michael R Harris
Jr Russell U Nesbitt
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Warner Lambert Co LLC
Original Assignee
Warner Lambert Co LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US06/696,955 external-priority patent/US4600645A/en
Application filed by Warner Lambert Co LLC filed Critical Warner Lambert Co LLC
Publication of GB8601389D0 publication Critical patent/GB8601389D0/en
Publication of GB2170104A publication Critical patent/GB2170104A/en
Withdrawn legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/5073Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals having two or more different coatings optionally including drug-containing subcoatings

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  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Epidemiology (AREA)
  • Medicinal Chemistry (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Medicinal Preparation (AREA)

Abstract

Coated pharmaceutical dosage forms comprises (1) a drug-containing substrate coated with a sustained release formulation, e.g. ethyl cellulose and (2) product of step (1) coated with a water-soluble overcoat, e.g. hydroxypropylmethycellulose or hydroxypropylcellulose. Substantial reductions in tackiness problems and curing times result when dosage forms are coated in this way.

Description

SPECIFICATION Process for treating pharmaceutical dosage forms Recently, owing to stringent government regulations and the safety hazards associated with the use of organic solvents in coating systems for dosage forms, emphasis has shifted from solvent-based to waterbased coating formulations. New polymeric dispersions have been developed and intensive research is being conducted to maximize the uses of water dispersible colloidai particles. However, these aqueous formulations have generally exhibited shortcomings during the coating process.
One major problem is the tackiness which occurs during the curing of polymeric coatings. Although elevated temperatures are required to drive off water rapidly and deposit a film on the product, usually moderate temperatures (300 - 50 ) are employed in order to avoid the tackiness that has been frequently observed. Once the product is coated, the deposited film requires treatment at lower temperatures for extended periods of time to fully coalesce the polymer beads and ensure a continuous film. If elevated temperatures are employed, coalescence time may be shortened and reproducible release profiles achieved. However, the film usually becomes tacky and makes product handling difficult.
According to the present invention, there is provided a process for treating a pharmaceutical dosage form, comprising the steps of: (1) coating a drug-containing substrate with a sustained release formulation, and (2) coating the product of step (1) with a water-soluble overcoat.
The present invention provides a process that substantially reduces or eliminates the tackiness problem, and significantly reduces the curing time for coatings from days down to minutes or hours. In accordance with the present invention, the product is first coated under suitable conditions using the appropriate sustained release formulation, followed, preferably immediately, by the provision of a watersoluble overcoat, for instance by spraying; thereafter the product temperature is elevated to the desired level. The process is continued until complete coalescence of the film is attained.
The optimum temperature and time to be used will depend upon the type of formulation, coating level and the type of polymeric dispersion. The overcoat is composed of a single agent or a combination containing one or more water-soluble, natural or synthetic polymers such a cellulosic derivatives, and polyethylene glycols. Pharmaceutically acceptable additives, such as talc or kaolin, may be added to the overcoat formulation to help reduce tackiness while the overcoat is applied.
In one preferred embodiment, drug pellets are coated with a sustained-release compositidn which contains ethyl cellulose, triethyl citrate, kaolin and water. The coated pellets are then heated to temperatures of the order of from 30"C to 70"C for a period of from 15 minutes to 3 hours.
An overcoat formulation containing hydroxypropyl methylcellulose, polyethylene glycol, talc and water is then applied to the pellets. The over-coated pellets do not exhibit the tackiness generally associated with coated dosage forms. The overcoat dries in from 5 to 10 minutes.
The process of the present invention can lead to several advantages over known processes of treating dosage forms. In addition to solving several handling problems, i.e. alleviating tackiness and slow curing, the process of the present invention can produce treated dosage forms whose release profiles are superior to those produced in accordance with known procedures.
Time and energy requirements can also be lessened when using the present invention. The coating process can be carried out using only one coating device, resulting in considerable savings.
The process of the present invention can include, as step (3), recovering the overcoated dosage form.
Substrates which can be coated in accordance with the inventive process encompass a wide variety of materials. While it is preferred that they contained one or more drugs as the principal active ingredients, other ingestible substances, e.g. vitamins, minerals, nutrients and the like, can be substituted for all or part of the drug(s) in the substrate.
Useful drugs include antihistamines, antihypertensives and tranquilizers. One preferred group of drugs to be treated includes antihistamines, such as diphenhydramine and pharmaceutically acceptable derivatives/precursors thereof. Diphenhydramine and diphenhydramine hydrochloride are highly preferred ingredients for inclusion in the drug-containing substrate. Other drugs whose taste or other characteristics dictate a need for delayed/sustained release, e.g. cholestyramine and procainamide and its salts, are operable.
The drug-containing substrate can also include one or more of a wide variety of additives conventionally employed in solid dosage forms, e.g. carriers, flavour enhancers, colourants, and the like. When such additives are employed, they are present in such quantities that the quantity of active ingredient, e.g.
drugs, which is present in the substrate is from about 5.0 to about 95.0 wt %, based on the total weight of the drug-containing substrate.
While the use of solid materials in the drug-containing substrate is preferred, the use of liquid ingredients, with or without suitable solid absorbents therefor, is also contemplated. The process of the invention is, with minor adjustment, suitable for treating liquid substrates.
The sustained release formulation The first coating applied to the drug containing substrate is particularly formulated so that, after the dosage form is ingested, the drug or other active ingredient contained in the substrate is taken up by the body in a slow and sustained fashion. That is, the dosage release curves which result from the use of the initial coating are smooth, almost linear, curves when cumulative percent release is plotted against time.
Suitable formulations for use in the initial coatings contain water soluble and/or water dispersible mat rices to which suitable ingredients have been added in order to reduce the tackiness and curing time of the coated substrate.
Typical matrices are polymeric materials such as cellulosic ethers. Aquacoat, made by FMC, is an ex ample of a highly preferred polymeric dispersion matrix. It is composed of ethylcellulose colloidal parti cles dispersed in water with cetyl alcohol and sodium lauryl sulfate added as stabilizers. Mixtures of matrices are operable.
Useful additives in the first coating include inert solids, e.g. clays and ion exchange materials which modify the release of the active ingredient from the substrate through the coating. Talc and kaolin are preferred.
Other additives, e.g. hydrophilic polymers such as polyethylene glycols can be employed. Triethyl cit rate, a plasticizer, is a preferred processing aid. Mixtures of such additives are contemplated.
The relative quantities of the matrix material in the sustained release coating will be on the order of about 50.0 to about 80.0 wt %, based in total coating solids weight. Other additives, if present, will com bine about 50.0 to about 20.0 wt %, based on total solids.
Since the coating is to be applied from an aqueous vehicle, solvents and other non-aqueous ingredi ents need not be used. The quantity of water present during the first coating operation depends upon such factors as the nature of the substrate and the type of equipment employed for the coating opera tion.
The hydrophilic overcoat The second coating composition, or overcoat, is designed to enhance the processability of the final product. It is the overcoat which significantly reduces the outlay in time and energy generally associated with treating the coated dosage forms.
The overcoat or second coating of the invention, like the first or base coat, is applied from an aqueous vehicle. The matrix of this second coating contains one or more hydrophilic, preferably highly water soluble materials of monomeric or polymeric nature. One preferred matrix is hydroxypropylmethyl cellu lose. Other suitable matrices include hydroxypropyl cellulose and the like. Mixtures are operable.
The use of hydrophilic matrices is preferred. However, non-hydrophilic matrices may be used in combi nation with suitable amounts of fillers to yield properties similar to those attained using hydrophilic mat rices. For instance, a water-insoluble hydrophilic polymer, e.g., an ethyi cellulose polymer containing major amounts--i.e., 30-90% of talc, kaolin or other filler, will give similar results as a hydrophilic over coat.
To assist in the flow properties of this coating when applied and in the subsequent handling of the overcoated dosage form, conventional processing aids, e.g., surfactants, fillers, etc. can be employed.
One preferred group of surfactants are silicon polymers. Polyethylene glycols and other well-known hy drophobic polymers are highly preferred as additives. Polyethylene glycol 3350 is particularly preferred when aqueous hydroxypropylmethy cellulose is the matrix.
Any of the optional ingredients employable in the base coating, described above, can be employed in the overcoat formulation. The amount of matrix material in the overcoat composition will range from about 0.01 to about 100% wt % based on total solids weight.
Coating procedures The two-step coating process carried out in accordance herewith can be effected using conventional coating equipment. Suitable devices for applying the initial, or base, coating include fluidized bed granu lation and drying devices and the like. The one preferred device is the Rotor Granulator made by Glatt.
In order to save time in the overall process, it is preferred that, following the initial coating step, the base-coated substrate be allowed to sit, with optional heat treatment to temperatures of about 45"C to about 70"C, and preferably about 55"C to about 60"C, to coaiesce the matrix particles, so that a useful film results. When heat is employed it is generally used for about 15 to about 60 minutes, preferably about 20 to about 40 minutes.
The application of the second, or overcoat, formulation can be carried out using the same equipment as was used for the base coat. One preferred embodiment requires the use of only one type of device with continuous coating steps.
The drying temperatures and times to be used on the overcoat will be about 30 to about 80"C, for about 2 to about 15 minutes. Generally, preferred temperatures and times are about 45 to about 60"C and about 5 to about 10 minutes, respectively. The drying parameters used in treating the based coating in termediate--i.e., the product of step (1 )will be operable in this step as well.
Recovery of the final dosage form is carried out using conventional techniques. Once the overcoat has dried, the treated dosage forms are processed via well-known operations, such as are generally em ployed to accommodate packaging and/or storage requirements.
Other conventional techniques for handling oral dosage forms can be employed before, during and/or after the two-step process outlined above.
The chemical and physical nature of the substrate will dictate the final form which the preparations of this invention will take. For example, diphenydramine hydrochloride is a bitter-tasting solid substance.
Since it is in antihistamine, it is an excellent candidate for applicants' process.
While ingestible pellets are preferred final product, other coated dosage forms, e.g. powders, capsules and the like, are also contemplated.
The following examples demonstrate the effectiveness of the invention.
Example I The coating formulations used in this example were: (a) Sustained-release (base) formulation 1. Aquacoat 465 gm 2. Triethylcitrate 186 gm 3. Kaolin 51 gm 4. Purified water 990 gm (b) Overcoat formulation 5. Hydroxypropylmethylcellulose 6.0 gm 6. Polyethylene Glycol 3350 1.2 gm 7. Talc 1.0 gm 8. Purified water 91.8 gm I. Sustained Release Coating: (Parameters for 5 kg of pellets) Use 0.564 kg of coating dispersion for 1 kg of pellets.
A. Disperse 3 in 4 and hydrate for 10 minutes.
B. Add A and 2 to 1 (in that order) and mix for 10 minutes after each addition.
C. Place the drug pellets into Glatt Rotor-Granulator container (5 kg in Glatt Model GPCG-5).
D. Coat C with B using 1.2 mm nozzle orifice, atomizing pressure set at 2.5 bars, flap opening = 40%, air inlet temperature = 45"C and bed temperature = 32-85"C, rotor = 250 rpm. Spray 8.0% of coating suspension at the rate of 4.0 ml/minute per 1 kg pellets. Spray remainder of the coating suspension at the rate of 10.0 ml/minute per 1 kg pellets.
II. Aqueous Overcoat: Use 0.415 kg of coating dispersion for 1 kg of core pellets.
E. Add 6 to about 90% of 8, heat to 60"C and sprinkle in 5. Cool to room temperature with mixing.
Continue mixing until dissolved. Disperse 7; continue mixing throughout the coating process.
F. Coat pellets from I in Rotor-Granulator with E immediately after the sustained release coating using a 1.2 mm nozzle orifice, atomizing pressure set at 2.5 bars, air inlet temperature = 65"C and bed temper ature = 45-50"C. Spray at the rate of 24 ml/minute per 1 kg of pellets. Dry the coated pellets for 30 min utes at an inlet air temperature of 70"C and rotor speed of 100 rpm.
The figure The figure depicts the release profiles of diphenhydramine pellets, a portion of which were cured at 60 for one hour only using the claimed procedure (lower curve) and another portion which were further stored at 60 for one more week in an oven (upper curve). The similarity of the curves underscores the efficiency of Applicants' curing process.
Reasonable variations, such as those which would occur to a skilled artisan, can be made herein with out departing from the scope of the invention.

Claims (10)

CLAIMS I
1. A process for treating a pharmaceutical dosage form, comprising the steps of: (1) coating a drug-containing substrate with a sustained release formulation, and (2) coating the product of step (1) with a water-soluble overcoat.
2. A process according to Claim 1, which also includes, as step (3), recovering the overcoated dosage form.
3. A process according to Claim 1 or 2, wherein the formulation employed in step (1) contains a water-dispersible polymer and an adsorbent.
4. A process according to Claim 1, 2, or 3, wherein the overcoat contains a water-soluble polymer.
5. A process according to Claim 4, wherein the overcoat additionally includes at least one processing aid.
6. A process according to Claim 5, wherein the processing aid is selected form adsorbents, plasticiz ers, and mixtures thereof.
7. A process according to any preceding claim, wherein the drug-containing substrate is a pellet.
8. A process according to any preceding claim, wherein the overcoat contains at least one hydrophoi bic polymer.
9. A process according to any preceding claim, wherein steps (1) and (2) are carried out in the same device without removal of the product of step (1) prior to commencement of step (2).
10. An overcoated dosage form produced by a process according to any preceding claim.
GB08601389A 1985-01-30 1986-01-21 Coated pharmaceutical dosage forms Withdrawn GB2170104A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US69694585A 1985-01-30 1985-01-30
US06/696,955 US4600645A (en) 1985-01-31 1985-01-31 Process for treating dosage forms

Publications (2)

Publication Number Publication Date
GB8601389D0 GB8601389D0 (en) 1986-02-26
GB2170104A true GB2170104A (en) 1986-07-30

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GB08601389A Withdrawn GB2170104A (en) 1985-01-30 1986-01-21 Coated pharmaceutical dosage forms

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Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0207041A2 (en) * 1985-06-12 1986-12-30 "Galephar" Pharmaceutical tablets for easy administration of pellets, their preparation and use
EP0339811A2 (en) * 1988-04-28 1989-11-02 Alza Corporation Aqueous based pharmaceutical coating composition for dosage forms
WO1992009270A1 (en) * 1990-11-22 1992-06-11 British Technology Group Ltd Controlled release compositions
WO1992011845A1 (en) * 1991-01-03 1992-07-23 Glaxo Canada Inc. Method for production of solid pharmaceutical preparation
EP0548448A1 (en) * 1991-12-24 1993-06-30 Euro-Celtique S.A. Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
US5472712A (en) * 1991-12-24 1995-12-05 Euroceltique, S.A. Controlled-release formulations coated with aqueous dispersions of ethylcellulose
US5681585A (en) * 1991-12-24 1997-10-28 Euro-Celtique, S.A. Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
US5683719A (en) * 1990-11-22 1997-11-04 British Technology Group Limited Controlled release compositions
US5958459A (en) * 1991-12-24 1999-09-28 Purdue Pharma L.P. Opioid formulations having extended controlled released
US6103261A (en) 1993-07-01 2000-08-15 Purdue Pharma Lp Opioid formulations having extended controlled release
US6306438B1 (en) 1997-07-02 2001-10-23 Euro-Celtique, S.A. Stabilized sustained release tramadol formulations
US6733783B2 (en) 2000-10-30 2004-05-11 Euro-Celtique S.A. Controlled release hydrocodone formulations
US7740881B1 (en) 1993-07-01 2010-06-22 Purdue Pharma Lp Method of treating humans with opioid formulations having extended controlled release
US7846476B2 (en) 2001-05-02 2010-12-07 Purdue Pharma L.P. Once-a-day oxycodone formulations
US7883722B2 (en) 1998-04-03 2011-02-08 Egalet Ltd. Controlled release composition
US7943174B2 (en) 1999-10-29 2011-05-17 Purdue Pharma L.P. Controlled release hydrocodone formulations
US8298581B2 (en) 2003-03-26 2012-10-30 Egalet A/S Matrix compositions for controlled delivery of drug substances
US8449914B2 (en) 2002-11-08 2013-05-28 Egalet Ltd. Controlled release carvedilol compositions
US8609143B2 (en) 2001-09-21 2013-12-17 Egalet Ltd. Morphine polymer release system
US8617605B2 (en) 2001-09-21 2013-12-31 Egalet Ltd. Polymer release system
US8877241B2 (en) 2003-03-26 2014-11-04 Egalet Ltd. Morphine controlled release system
US9005660B2 (en) 2009-02-06 2015-04-14 Egalet Ltd. Immediate release composition resistant to abuse by intake of alcohol
US9023394B2 (en) 2009-06-24 2015-05-05 Egalet Ltd. Formulations and methods for the controlled release of active drug substances
US9044402B2 (en) 2012-07-06 2015-06-02 Egalet Ltd. Abuse-deterrent pharmaceutical compositions for controlled release
US9642809B2 (en) 2007-06-04 2017-05-09 Egalet Ltd. Controlled release pharmaceutical compositions for prolonged effect
US9655893B2 (en) 2001-05-02 2017-05-23 Purdue Pharma L.P. Once-a-day oxycodone formulations
US10179130B2 (en) 1999-10-29 2019-01-15 Purdue Pharma L.P. Controlled release hydrocodone formulations

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB931150A (en) * 1958-12-22 1963-07-10 Upjohn Co A process for the two-fold encapsulation of hydrophilic material by phase separation
GB1179938A (en) * 1966-11-23 1970-02-04 Merck & Co Inc Medicinal Sustained-Release Tablets.
EP0122077A2 (en) * 1983-04-06 1984-10-17 ELAN CORPORATION, Plc Sustained absorption pharmaceutical composition
EP0123470A1 (en) * 1983-04-21 1984-10-31 ELAN CORPORATION, Plc Controlled absorption pharmaceutical composition

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB931150A (en) * 1958-12-22 1963-07-10 Upjohn Co A process for the two-fold encapsulation of hydrophilic material by phase separation
GB1179938A (en) * 1966-11-23 1970-02-04 Merck & Co Inc Medicinal Sustained-Release Tablets.
EP0122077A2 (en) * 1983-04-06 1984-10-17 ELAN CORPORATION, Plc Sustained absorption pharmaceutical composition
EP0123470A1 (en) * 1983-04-21 1984-10-31 ELAN CORPORATION, Plc Controlled absorption pharmaceutical composition

Cited By (76)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0207041A3 (en) * 1985-06-12 1988-03-16 "Galephar" Pharmaceutical tablets for easy administration of pellets, their preparation and use
EP0207041A2 (en) * 1985-06-12 1986-12-30 "Galephar" Pharmaceutical tablets for easy administration of pellets, their preparation and use
EP0339811A2 (en) * 1988-04-28 1989-11-02 Alza Corporation Aqueous based pharmaceutical coating composition for dosage forms
EP0339811A3 (en) * 1988-04-28 1990-11-07 Alza Corporation Aqueous based pharmaceutical coating composition for dosage forms
US5683719A (en) * 1990-11-22 1997-11-04 British Technology Group Limited Controlled release compositions
WO1992009270A1 (en) * 1990-11-22 1992-06-11 British Technology Group Ltd Controlled release compositions
WO1992011845A1 (en) * 1991-01-03 1992-07-23 Glaxo Canada Inc. Method for production of solid pharmaceutical preparation
US5681585A (en) * 1991-12-24 1997-10-28 Euro-Celtique, S.A. Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
US6129933A (en) * 1991-12-24 2000-10-10 Purdue Pharma Lp Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
AU680491B2 (en) * 1991-12-24 1997-07-31 Euro-Celtique S.A. Controlled release formulations coated with aqueous dispersions of ethyl cellulose
US7316821B2 (en) 1991-12-24 2008-01-08 Purdue Pharma, L.P. Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
US5273760A (en) * 1991-12-24 1993-12-28 Euroceltigue, S.A. Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
US5958459A (en) * 1991-12-24 1999-09-28 Purdue Pharma L.P. Opioid formulations having extended controlled released
US6905709B2 (en) 1991-12-24 2005-06-14 Purdue Pharma, Lp Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
US5472712A (en) * 1991-12-24 1995-12-05 Euroceltique, S.A. Controlled-release formulations coated with aqueous dispersions of ethylcellulose
EP0548448A1 (en) * 1991-12-24 1993-06-30 Euro-Celtique S.A. Stabilized controlled release substrate having a coating derived from an aqueous dispersion of hydrophobic polymer
US6143322A (en) 1993-07-01 2000-11-07 Purdue Pharma L.P. Method of treating humans with opioid formulations having extended controlled release
US6103261A (en) 1993-07-01 2000-08-15 Purdue Pharma Lp Opioid formulations having extended controlled release
US7740881B1 (en) 1993-07-01 2010-06-22 Purdue Pharma Lp Method of treating humans with opioid formulations having extended controlled release
US6306438B1 (en) 1997-07-02 2001-10-23 Euro-Celtique, S.A. Stabilized sustained release tramadol formulations
US6645527B2 (en) 1997-07-02 2003-11-11 Euro-Celtique S.A. Stabilized sustained release tramadol formulations
US7883722B2 (en) 1998-04-03 2011-02-08 Egalet Ltd. Controlled release composition
US8980291B2 (en) 1999-10-29 2015-03-17 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9675611B1 (en) 1999-10-29 2017-06-13 Purdue Pharma L.P. Methods of providing analgesia
US7943174B2 (en) 1999-10-29 2011-05-17 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9320717B2 (en) 1999-10-29 2016-04-26 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9278074B2 (en) 1999-10-29 2016-03-08 Purdue Pharma L.P. Controlled release hydrocodone formulations
US10179130B2 (en) 1999-10-29 2019-01-15 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9056107B1 (en) 1999-10-29 2015-06-16 Purdue Pharma L.P. Controlled release hydrocodone formulations
US10076516B2 (en) 1999-10-29 2018-09-18 Purdue Pharma L.P. Methods of manufacturing oral dosage forms
US9669022B2 (en) 1999-10-29 2017-06-06 Purdue Pharma L.P. Controlled release hydrocodone formulations
US8975273B2 (en) 1999-10-29 2015-03-10 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9669024B2 (en) 1999-10-29 2017-06-06 Purdue Pharma L.P. Controlled release hydrocodone formulations
US6733783B2 (en) 2000-10-30 2004-05-11 Euro-Celtique S.A. Controlled release hydrocodone formulations
US9056052B1 (en) 2000-10-30 2015-06-16 Purdue Pharma L.P. Controlled release hydrocodone formulations
US8647667B2 (en) 2000-10-30 2014-02-11 Purdue Pharma, L.P. Controlled release hydrocodone formulations
US9682077B2 (en) 2000-10-30 2017-06-20 Purdue Pharma L.P. Methods of providing analgesia
US8951555B1 (en) 2000-10-30 2015-02-10 Purdue Pharma L.P. Controlled release hydrocodone formulations
US10022368B2 (en) 2000-10-30 2018-07-17 Purdue Pharma L.P. Methods of manufacturing oral formulations
US9517236B2 (en) 2000-10-30 2016-12-13 Purdue Pharma L.P. Controlled release hydrocodone formulations
US8551520B2 (en) 2000-10-30 2013-10-08 Purdue Pharma L.P. Controlled release hydrocodone
US9023401B1 (en) 2000-10-30 2015-05-05 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9669023B2 (en) 2000-10-30 2017-06-06 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9572804B2 (en) 2000-10-30 2017-02-21 Purdue Pharma L.P. Controlled release hydrocodone formulations
US8715721B2 (en) 2000-10-30 2014-05-06 Purdue Pharma L.P. Controlled release hydrocodone
US8361499B2 (en) 2000-10-30 2013-01-29 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9060940B2 (en) 2000-10-30 2015-06-23 Purdue Pharma L.P. Controlled release hydrocodone
US9198863B2 (en) 2000-10-30 2015-12-01 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9205055B2 (en) 2000-10-30 2015-12-08 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9205056B2 (en) 2000-10-30 2015-12-08 Purdue Pharma L.P. Controlled release hydrocodone formulations
US8231898B2 (en) 2000-10-30 2012-07-31 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9289391B2 (en) 2000-10-30 2016-03-22 Purdue Pharma L.P. Controlled release hydrocodone formulations
US8142811B2 (en) 2000-10-30 2012-03-27 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9572805B2 (en) 2000-10-30 2017-02-21 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9526724B2 (en) 2000-10-30 2016-12-27 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9504681B2 (en) 2000-10-30 2016-11-29 Purdue Pharma L.P. Controlled release hydrocodone formulations
US9655893B2 (en) 2001-05-02 2017-05-23 Purdue Pharma L.P. Once-a-day oxycodone formulations
US10660886B2 (en) 2001-05-02 2020-05-26 Purdue Pharma L.P. Oxycodone formulations
US9750736B2 (en) 2001-05-02 2017-09-05 Purdue Pharma L.P. Oxycodone formulations
US7846476B2 (en) 2001-05-02 2010-12-07 Purdue Pharma L.P. Once-a-day oxycodone formulations
US8808745B2 (en) 2001-09-21 2014-08-19 Egalet Ltd. Morphine polymer release system
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