Controlled release pharmaceutical preparation and method for producing the same.
Abstract
Disclosed is a controlled release pharmaceutical preparation, comprising a core containing a pharmaceutically active ingredient, and a porous film of a hydrophobic polymeric substance or a hydrophobic polymeric substance and a hydrophilic polymeric substance, the core being coated with the porous film. Also disclosed is a method for producing the same.

Term
Term ended
Projected expiry passed 21 March 2009, 17.5 years ago.
- Priority
- Filed
- Published
- Projected expiry
- Today
11 claims: 7 independent, 4 dependent
- 1A controlled release pharmaceutical preparation characterised by a core containing a pharmaceutically active ingredient, and a porous film of a hydrophobic polymeric substance or a hydrophobic polymeric substance and a hydrophilic polymeric substance, said core being coated with said porous film.
- 6A preparation according to any of claims 1 to 5, characterised in that the hydrophilic substance is at least one selected from the group consisting of water soluble polymeric substances, enteric polymeric substances, gastric soluble polymeric substances and both gastric soluble and enteric polymeric substances.
- 11A method for producing a controlled release pharmaceutical preparation, which comprises spray coating a core containing a pharmaceutically active ingredient with a water-organic solvent mixture containing a hydrophobic polymeric substance of a hydrophobic polymeric substance and a hydrophilic polymeric substance to form a porous film comprising said polymeric substance or substances on the surface of the core.
Independent claims7
80 paragraphs, as filed
This invention relates to a novel controlled release pharmaceutical preparation and a method for producing the same.
Heretofore, there has been known pharmaceutical preparations in which drug-containing cores are coated with compact films of hydrophobic polymeric substances.
Such preparations have advantages that they have excellent water resistance, light resistance, humidity resistance, abrasion resistance, storage stability, etc.
However, a preparation having a compact film of a hydrophobic substance has disadvantages that it is slow in releasing rate of the inner drug and also that the drug cannot be completely released.
In other words, release of a drug is owing to the difference in concentration or osmotic pressure between the inside and outside of the preparation which is created by the dissolution of the drug to saturated concentration with digestive fluids having penetrated into the inside through the film. However, since the compact film of a hydrophobic substance scarcely has open space, permeation of the fluid into the film is slow, and even when an osmotic pressure difference enough to release the drug to outside may be created, the dissolution speed is not sufficient because of the small total area of the open space contributing to release.
As the method for solving this problem, there has been known a method in which particles of a water-soluble substance are embedded in the film of a hydrophobic polymeric substance so that the film may become porous in digestive organs by dissolution and elimination of said water-soluble substance.
However, this method is still disadvantageous in that a special contrivance is required for embedding a water-soluble substance in the film, and that it is necessary to use various additives such as dispersing agents, plasticizers, anti-aggregating agents, etc. which make the recipe complicated. Moreover, even if the film may become porous in digestive organs, its porosity will be affected by the particle size of the water-soluble substance or the degree of dispersion of said substance in the film, and therefore the porosity cannot be necessarily controlled accurately.
The present inventors have studied intensively in order to enable release control while maintaining the advantages of a preparation having a compact film of a hydrophobic polymeric substance such as great physical strength, good storage stability, etc. As a result, the inventors have succeeded in forming a porous film of a hydrophobic polymeric substance on the surface of a core, and also found that a controlled release pharmaceutical preparation having a desired dissolution rate can be obtained by controlling the porosity of the film.
Namely, according to the present invention, there is provided a controlled release pharmaceutical preparation comprising a core containing a pharmaceutical active ingredient, and a porous film of a hydrophobic polymeric substance, said core being coated with said porous film. Further, there is provided a method for producing said preparation.
In the present invention, the core to be coated with the porous film is not particularly limited to specific form, but any of forms such as plain tablets, pills, granules, grains, etc. can be suitably used. However, it is preferable to use one granulated into granules, grains, etc., preferably one granulated into granules with an average particle size of about 300 µm to about 2000 µm, particularly about 500 µm to about 850 µm. The core of the present invention is not required to be hydrophobic, but both water-soluble core and water-insoluble core can be suitably used.
The core may contain a wide variety of excipients including diluents, binders, lubricants, anti-aggregating agents, buffers, which are conventionally used in this field of art. For example, as the diluents, sugars such as sucrose, lactose, mannitol, glucose, etc., starch, crystalline cellulose, calcium phosphate, calcium sulfate, calcium lactate, etc. may be included; as the binders, polyvinyl alcohol, polyacrylic acid, polymethacrylic acid, polyvinyl pyrrolidone, glucose, sucrose, lactose, maltose, sorbitol, mannitol, hydroxyethyl cellulose, hydroxypropylmethyl cellulose, hydroxypropyl cellulose, polyethylene glycols, gum arabic, gelatin, agar, starch, etc. As the lubricants and anti-aggregating agents, talc, magnesium stearate, calcium stearate, colloidal silica, stearic acid, waxes, hardened oil, polyethylene glycols, sodium benzoate, sodium laurylsulfate, magnesium laurylsulfate, etc. may be included. Furhter, as the buffers, organic acids such as fumaric acid, succinic acid, citric acid, malic acid and their salts may be included.
The hydrophobic polymeric substance constituting the porous film is not particularly limited, provided that it has film forming ability, and is insoluble in water, but soluble in a water-miscible organic solvent. Examples of such hydrophobic polymeric substance may include cellulose ether, cellulose ester, polyvinyl ester, acrylic acid type polymer having a quaternaly ammonium-alkyl group, etc. Specifically, there may be included, for example, ethyl cellulose, butyl cellulose, cellulose acetate, cellulose propionate; polyvinyl acetate, polyvinyl butyrate; Eudragit RS (trade name of Röhm Pharma, chemical name: ethyl acrylate-methyl methacrylate-ethyl ammonium trimethyl chloride methacrylate copolymer), etc., and among them, preferable hydrophobic polymeric substances may include, for example, ethyl cellulose, butyl cellulose, cellulose acetate, cellulose propionate or Eudragit RS, etc. Among them, ethyl cellulose and cellulose acetate are particularly preferred, and most preferable is ethyl cellulose. Ethyl cellulose may be above all preferably a water-insoluble ethyl cellulose having, for example, an ethoxy content of about 40 to about 55%, particularly about 43% to about 51%, with a viscosity [viscosity measured at 5% ethyl cellulose concentration in toluene-ethanol (4:1) mixture at 25 °C] of about 4 to about 350 cP.
The porous film in the present invention may be, other than a porous film comprising only a hydrophobic polymeric substance, a porous film comprising a hydrophobic polymeric substance and a hydrophilic polymeric substance. In this case, as the hydrophilic polymeric substance, a water-soluble polymeric substance, an enteric polymeric substance, a gastric souble polymeric substance, and a both gastric and enteric polymeric substance may be suitably used.
Examples of the water-soluble polymeric substance, may include polysaccharides optionally having sulfuric acid group such as pullulan, dextrin, alkali metal alginate, etc.; polysaccharides having a hydroxy-alkyl group or a carboxyalkyl group such as hydroxypropyl cellulose, hydroxypropylmethyl cellulose, carboxymethyl cellulose sodium, etc.; methyl cellulose, polyvinyl pyrrolidone, polyvinyl alcohol or polyethylene glycol, etc. may be included. Among them, more preferable water soluble polymeric substances may include hydroxypropyl cellulose or polyethylene glycol.
As the enteric polymeric substance, a polymeric substance having film forming ability and being soluble in water of pH 5 or higher may be used, including, for example, (1) carboxyalkyl cellulose, (2) cellulose derivative having monoester bond of dibasic acid, (3) polyvinyl derivative having monoester bond of dibasic acid, (4) maleic acid-vinyl copolymer or (5) acrylic acid type polymer, etc. Specific examples of (1) may include carboxymethyl cellulose; specific examples of (2) may include cellulose acetate phthalate, cellulose acetate succinate, methylcellulose phthalate, hydroxymethyl ethyl cellulose phthalate, hydroxypropylmethyl cellulose phthalate, hydroxypropylmethyl cellulose acetate succinate and the like; specific examples of (3) may include dibasic acid monoesters of vinyl polymers such as polyvinyl alcohol phthalate, polyvinyl butyrate phthalate, polyvinyl acetoacetal phthalate and the like; specific examples of (4) may include vinyl acetate-maleic anhydride copolymer, vinyl butyl ether-maleic anhydride copolymer, styrene-maleic acid monoester copolymer; and specific examples of (5) may include methyl acrylate-methacrylic acid copolymer, styrene-acrylic acid copolymer, methyl acrylate-methacrylic acid-octyl acrylate copolymer, Eudragit L and S (trade names of Rhom-Pharma, methacrylic acid-methyl methacrylate copolymer), etc. Among them, more preferable enteric polymeric substances are carboxylmethyl cellulose, hydroxypropyl methyl cellulose acetate succinate or Eudragit L.
Further, as the gastric soluble polymeric substance, any polymeric substance soluble in water of pH 6 or lower and having film forming ability may be used, including, for example, (a) cellulose derivaive having mono- or di-substituted amino group, (b) polyvinyl derivative having mono- or di-substituted amino group, (c) acrylic acid polymer having mono-substituted amino group, etc. Specific examples of (a) may include benzylaminomethyl cellulose, diethylaminomethyl cellulose, piperidyl ethyl hydroxyethyl cellulose, cellulose acetate diethylamino acetate, etc. Specific examples of (b) may include vinyldiethylamine-vinyl acetate copolymer, vinylbenzylamine-vinyl acetate copolymer, polyvinyl acetaldiethylaminoacetate, vinylpiperidyl-acetoacetalvinyl acetate copolymer, polydiethyl aminomethyl styrene, etc., and specific examples of (c) may include Eudragit E (trade name of Rohm-Pharma, methyl methacrylate-butyl methacrylate-dimethylaminoethyl methacrylate copolymer), polydimethylaminoethyl methacrylate, etc. Among these, more preferable gastric soluble polymeric substances are polyvinyl acetal-diethylaminoacetate or Eudragit E.
As the both gastric soluble and enteric polymeric substance, a polymeric substance having film forming ability and being soluble in water of pH 4.5 or lower and water of pH 6 or higher may be used, including vinylpyridine-acrylic acid type copolymer, carboxymethyl polysaccharide having mono- or di-substituted amino group or polyvinyl amino acid type derivative. Specific examples of vinylpyridine-acrylic acid type copolymer may include 2-methyl-5-vinylpyridine/methyl methacrylate/ methacrylic acid copolymer, 2-methyl-5-vinylpyridine/ methyl acrylate/methacrylic acid copolymer, 2-vinyl-5-ethyl pyridine/methacrylic acid/styrene copolymer, 2-vinyl-5-ethyl pyridine/methacrylic acid/methyl acrylate copolymer, 2-vinylpyridine/methacrylic acid/methyl acrylate copolymer, 2-vinylpyridine/methacrylic acid/ acrylonitrile copolymer, etc. Specific examples of carboxymethyl polysaccharides having mono- or di-substituted amino group may include carboxymethyl piperidyl starch, carboxymethyl benzylaminocellulose, etc., and specific examples of polyvinyl amino acid type derivative may include poly-2-(vinylphenyl)glycine, N-vinylglycine-styrene copolymer, etc.
The combination of the hydrophobic polymeric substance and the hydrophilic polymeric substance is not particularly limited, but as preferable combination, a combination of a hydrophobic polymeric substance with a water soluble polymeric substance or an enteric polymeric substance may be included. As particularly preferable combination, a combination of ethyl cellulose with hydroxypropylcellulose, carboxymethylethyl cellulose or hydroxypropylmethyl cellulose acetate succinate may be employed. The ratio of the hydrophobic polymeric substance to the hydrophilic polymeric substance should be desirably about 0.05 to 0.5 part by weight of the hydrophilic polymeric substance per 1 part by weight of the hydrophobic polymeric substance.
The porous film comprising the hydrophobic polymeric substance or a combination of the hydrophobic polymeric substance and the hydrophilic polymeric substance has generally an appearance like sponge, and has regular or irregular pores of microscopic sizes, which are mutually communicated to each other.
The porosity of the porous film is represented by the formula (I):<maths id="math0001" num=""><img file="EP0335560A2_D0001.tif" /></maths> In general, the porosity should be appropriately made a value of about 0.4 to 0.9, particularly 0.5 to 0.85.
The thickness of the film may be controlled by the amount of the hydrophobic polymeric substance relative to the core, and it is desirable that the hydrophobic polymeric substance should be used in an amount within the range from about 3 to 100 W/W%, particularly about 5 to 50 W/W% based on the core. When the hydrophobic polymeric substance is used in combination with the hydrophilic polymeric substance, the total amount of both polymeric substances should be desirably within the range mentioned above.
In the preparation of the present invention, by controlling adequately the thickness and the porosity, it is possible to make a preparation having a desired dissolution rate. For examle, when the pharmaceutically active ingredient contained in the core is a drug which is desired to exhibit pharmaceutical effect within a short period of time after administration, it is preferred to make the film thinner and the porosity thereof greater, while in the case of a drug which is desired to be released persistently for a prolonged period of time, it is preferred to make the film thicker and the porosity thereof smaller.
As the pharmaceutically active ingredient to be contained in said core, any drug capable of oral administration may be available without limitation at all. Examples of such pharmaceutically active ingredients may include vitamins, amino acids, peptides, chemotherapeutics, antibiotics, agents affecting respiratory organs, antitussive expectorants, antitumor agents, autonomic drugs, neuropsychotropic agents, muscle relaxants, drugs affecting digestive organs, antihistamic agents, antidotes, hypnotic sedatives, antiepileptics, antipyretic analgesic antiphlogistics, cardiotonics, antiarrhythmics, hypotensive diuretics, vasodilators, hypolipidemic agents, alimentary analeptics, anticoagulants, hepatics, blood sugar-lowering agents, hypotensive agents, etc.
The preparation of the present invention can be produced by spray coating a core containing a pharmaceutically active ingredient with a water-organic solvent mixture containing a hydrophobic polymeric substance or a mixture of a hydrophobic polymeric substance and a hydrophilic polymeric substance to form a porous film of said polymeric substance or substances on the surface of the core.
Preparation of a core can be practiced according to conventional methods as described in Remington's Pharmaceutical Science 17th ed., p.p. 1603 to 1632, p.p 1633 to 1643 (Mark Publishing Company, published in 1985). For example, the core can be prepared by mixing a pharmaceutical compound with a suitable excipient or excipients (i,e., diluents, binders, lubricants, etc.) and then granulation the mixture according to the wet extrusion granulating method, the rotating granulation method, the fluidized bed granulation method, etc. Alternatively, the core can be prepared according to the rotating granulation method, the pan coating method, the fluidized bed coating method, etc. in which a pharmaceutical compound or a mixture of the compound with an excipient or excipients is added little by little to inert carrier particles while spraying a solution of a binder dissolved in a suitable solvent such as water, lower alcohol (methanol, ethanol, propanol, isopropanol, butanol, etc.), lower alkanone (acetone, methyl ethyl ketone, etc.), chloroform, dichloromethane, dichloroethane or a mixture of these on the surface of inert carrier particles. In this case, as the inert carrier particles, for example, those prepared from sucrose, lactose, starch, crystalline cellulose, etc. may be suitably employed. Such carrier particles should preferably have an average particle size of about 300 µm to about 1500 µm.
In coating the core with a porous film, as the organic solvent which forms a solvent mixture together with water, any solvent which can dissolve the hydrophobic polymeric substance can be used without particular limitation, including, for example, lower alkanols such as methyl alcohol, ethyl alcohol, isopropyl alcohol, n-propyl alcohol, n-butyl alcohol, etc., lower alkanones such as acetone, methyl ethyl ketone, etc., acetonitrile and so on. Among these, more preferable solvent is lower alkanols, and particularly preferable solvents are ethyl alcohol and isopropyl alcohol. The mixing ratio of water and the organic solvent is suitably variable within the range of 9 to 0.5 volumes of the organic solvent per one volume of water, and the porosity of the porous film comprising the hydrophobic polymeric substance or the combination of the hydrophobic polymeric substance and the hydrophilic polymeric substance can readily be controlled by changing said ratio. The porosity of the porous film, as a general rule, becomes greater as the ratio of water in the water-organic solvent mixture is increased and smaller when the ratio of the organic solvent is increased.
The concentration of the hydrophobic polymeric substance in the water-organic solvent mixture should be preferably about 2 to 30 W/W%. Also, when a hydrophobic polymeric substance is used in combination with a hydrophilic polymeric substance, the total concentration of the both polymeric substances should be preferably within the above range.
Spray coating can be practiced according to conventional coating method. For example, it can be practiced easily by dissolving a hydrophobic polymeric substance or a combination of a hydrophobic polymeric substance and a hydrophilic polymeric substance in a water-organic solvent mixture, and spraying the resultant coating solution on the surface of a core according to the fluidized bed coating method, the pan coating method, etc. For example, according to the pan coating method, it is possible to practice the method by placing cores in a coating pan, spraying a water-organic solvent mixture containing a hydrophobic polymeric substance or a combination of a hydrophobic polymeric substance and a hydrophilic polymeric substance through a nozzle of a spray gun while rotating said coating pan, and then drying the coating.
At this time, if desired, talc, titanium dioxide, etc. may be also added as the anti-aggregating agent.
The thus-obtained pharmaceutical preparation of the present invention may be administered as such or said preparation can be also administered in the form of capsules filled with it when the preparation is in shape of granules.
The controlled release pharmaceutical preparation of the present invention is characterized in that it shows rapid stand-up of release. This is because, since the film is porous, digestive fluids penetrate into the inside of the preparation and dissolve the pharmaceutically active ingredient from the time immediately after administration. Besides, the preparation of the present invention is characterized in that the release rate can be readily controlled by changing the porosity of the film. For example, in the case where it is necessary to reduce the variation of blood level of the pharmaceutically active ingredient because the minimum therapeutically effective blood level of said active ingredient is close to the toxic blood level thereof, it is possible to minimize the variation between the highest and lowest blood cocentration thereof by making the porosity of the film smaller in order to exhibit the therapeutic effect of the active ingredient while keeping the blood level thereof lower than the toxic level. Further, in the case where the pharmaceutically active ingredient is desired to show long-lasting action, it is possible to release the active ingredient at a constant rate for a prolonged period of time by making the porosity of the film smaller. On the other hand, in the case where the active ingredient is desired to show quick action, it is possible to release the active ingredient from the time immediately after administration by making the porosity of the film greater.
Moreover, the pharmaceutical preparation having a porous film comprising a hydrophobic polymeric substance and a hydrophilic polymeric substance is effective to dissolve and release the pharmaceutical ingredient more quickly and within a shorter period of time after administration because the porosity of the film itself becomes further greater by dissolution of the hydrophilic substance constituting a part of the porous film.
Besides, the preparation of the present invention is not inferior at all with respect to humidity resistance, light shielding property, water resistnce, abrasion resistance as compared with the known preparation having a compact film of a hydrophobic polymeric substance.
As described above, the preparation of the present invention is excellent in release control and at the same time, maintains the advantages possesed by the preparattion of the prior art as such.
Experimental examples
(1) Production of preparation:
One kg of Nonpareil (trade name of spherical granules of sucrose, manufactured by Freund) with particle sizes of 710 to 840 µm was placed and tumbled in a centrifugal fluidizing granulator (CF-360 EX Model, manufactured by Freund), and thereto was gradually added 1 kg of dilthiazem hydrochloride powder while spraying a water-ethanol solution (weight ratio=3:1) containing 400 g of sucrose to cover it around Nonpareil. Subsequently, the dilthiazem hydrochloride granules obtained were sprayed with a coating solution of 300 g of ethyl cellulose (ethoxy content: 49.6%) dissolved in 2.7 kg of a water-ethanol mixture (weight ratio=3:7, 2:8 or 1.5:8.5) while blowing warm air. By drying after spraying, dilthiazem hydrochloride containing preparations having porous ethyl cellulose films with different porosities, respectively, were obtained.
(2) Comparison of releasing rate:
For the respective preparations obtained as described above, the dissolution tests were practiced according to the dissolution test standard of the Paddle method specified in the 11th revised Japanese Pharmacopoeia.
(3) Results:
The dissolution percentage of the active ingredient (dilthiazem hydrochloride) is as shown in Table 1. <tables id="tabl0001" num="0001"><img file="EP0335560A2_D0002.tif" /></tables><tables id="tabl0002" num="0002"><img file="EP0335560A2_D0003.tif" /></tables>
As is apparent from the above Table 1, it can be seen that as the ratio of water in the water-ethanol mixture becomes smaller, the porosity of the film becomes smaller and a period of time to be required for dissolving 100% of the active ingredient become longer.
Example 1
500 g of Nonpareil with particle sizes of 710 to 840 µm were placed and tumbled in a centrifugal fluidizing granulator, and to this was gradually added 1 kg of theophylline (chemical name: 3,7-dihydro-1,3-dimethyl-1H-purine-2,6-dione) fine powder while spraying a solution of 270 g of sucrose dissolved in 145 ml of water to cover it around Nonpareil. Subsequently, 1 kg of the theophylline granules obtained was placed and tumbled in a centrifugal fluidizing granulator, and to this was sprayed a solution of 90 g of ethyl cellulose and 10 g of hydroxypropyl cellulose dissolved in 1.9 kg of a water-ethanol (3:7) mixture while blowing warm air. Subsequently, after drying, 1.1 kg of theophylline granules coated with a porous ethylcellulose-hydroxypropylcellulose film were obtained.
The preparation obtained had a porous film of a porosity of 0.81.
Example 2
One kg of Nonpareil with particle sizes of 710 to 840 µm was placed and tumbled in a centrifugal fluidizing granulator, and to this was added gradually 1 kg of sodium salicylate powder while spraying 800 g of a water-ethanol mixture containing 400 g of sucrose to have it attached around Nonpareil. Subsequently, 500 g of the sodium salicylate granules obtained were placed in a fluidized bed coater and, under blow rotation with blowing of air, a mixture of 100 g of ethyl cellulose dissolved in 900 g of a water-ethanol (2:8) mixture added with 50 g of talc was sprayed thereon while blowing warm air. By drying after spraying, 600 g of sodium salicylate granules coated with a porous ethyl cellulose film were obtained. The preparation obtained had a porous film of a porosity of 0.68.
Example 3
1.33 kg of Nonpareil with particle sizes of 500 to 710 µm were placed and tumbled in a centrifugal fluidizing granulator, and to this was gradually added a mixture of 1 kg of (+)-(2S,3S)-3-acetoxy-8-chloro-5-[2-(dimethylamino)ethyl]-2,3-dihydro-2-(4-methoxyphenyl)-1,5-benzodiazepine-4(5H)-one maleate fine powder and 1.67 g of succinic acid while spraying a solution of 652 g of sucrose dissolved in 1,957 g of a water-ethanol (3:1) mixture to cover it around Nonpareil. Subsequently, 2 kg of the granules obtained were placed and tumbled in a centrifugal fluidizing granulator, and a solution of 190 g of ethyl cellulose and 10 g of hydroxypropyl cellulose dissolved in 1.8 kg of a water-ethanol (3:7) mixture was sprayed thereon, while blowing warm air. Then, after drying, 2.2 kg of granules coated with a porous ethyl cellulose-hydroxypropyl cellulose film wereobtained.
The preparation obtained had a porous film of a porosity of 0.85.
Example 4
A mixture of 300 g of dilthiazem hydrochloride, 611 g of lactose and 150 g of corn starch was kneaded with 30 g of polyvinyl pyrrolidone and 100 ml of water, and the particles obtained were classified to obtain granules for tabletting. Then, to the granules were added 8 g of magnesium stearate, and the mixture was tabletted by a rotary system tabletting machine (RT F-9-2 Model, manufactured by Kikusui Seisakusho) to obtain tablets of 8 mm in diameter. The dilthiazem hydrochloride containing tablets obtained (500 g) were placed in a coating pan, and a water-ethanol (3:7) mixture containing 5 W/W% of ethyl cellulose was sprayed thereon at room temperature. Subsequently, after drying, tablets coated with a porous ethyl cellulose film were obtained.
The preparaton obtained had a porous film of a porosity of 0.67.
Example 5
500 g of theophylline granules (cores) obtained in the same manner as in Example 1 were placed in a centrifugal fluidizing granulator, and a solution of 50 g of ethyl cellulose dissolved in a water-isopropanol mixture (4:6) was sprayed thereon while blowing warm air. Subsequently, after drying, about 500 g of granules coated with a porous ethyl cellulose film were obtained.
The preparation obtained had a porous film of a porosity of 0.78.
Example 6
500 g of sodium salicylate granules (cores) obtained in the same manner as in Example 2 were placed in a fluidized bed coating device. 50 g of talc were added to a solution of 100 g of cellulose acetate in 900 g of a mixture of water-acetone (2:8), and the mixture was sprayed on the surface of granules while blowing warm air. By drying after spraying, 600 g of granules coated with a porous cellulose acetate film were obtained.
The granules obtained had a porous film of a porosity of 0.74.
Example 7
Example 1 was repeated except for using 100 g of cellulose acetate butyrate in place of cellulose acetate to obtain 600 g of granules coated with a porous cellulose acetate butyrate film.
The preparation obtained had a porous film of a porosity of 0.78.
Examples 8
One kg of the granules (cores) obtained in the same manner as in Example 3 was placed and tumbled in a centrifugal fluidizing granulator, and a solution of 95 g of ethyl cellulose and 5 g of polyvinyl pyrrolidone dissolved in 900 g of a water-ethanol (3:7) mixture was sprayed thereon while blowing warm air. By drying after spraying, 1.1 kg of granules coated with a porous ethyl cellulose-polyvinyl pyrrolidone film were obtained.
The preparation obtained had a porous film of a porosity of 0.81.
Example 9
Example 8 was repeated except for using 95 g ethyl cellulose and 5 g of polyethylene glycol to give 1.1 kg of granules coated with a porous ethyl cellulose-polyethylene glycol film.
The preparation obtained had a porous film of a porosity of 0.79.
Example 10
Example 8 was repeated except for using 95 g ethyl cellulose and 5 g of methyl cellulose to give 1.1 kg of granules coated with a porous ethyl cellulose-methylcellulose film.
The preparation obtained had a porous film of a porosity of 0.82.
Example 11
Example 8 was repeated except for using 95 g ethyl cellulose and 5 g of hydroxypropylmethyl cellulose to give 1.1 kg of granules coated with a porous ethyl cellulose-hydroxypropylmethyl cellulose film.
The preparation obtained had a porous film of a porosity of 0.76.
Example 12
Example 8 was repeated except for using 95 g ethyl cellulose and 5 g of hydroxypropyl cellulose acetate succinate to give 1.1 kg of granules coated with a porous ethyl cellulose-hydroxypropyl cellulose acetate succinate film.
The preparation obtained had a porous film of a porosity of 0.84.
Example 13
Example 8 was repeated except for using 95 g ethyl cellulose and 5 g of Eudragit L to give 1.1 kg of granules coated with a porous ethyl cellulose-Eudragit L film.
The preparation obtained had a porous film of a porosity of 0.79.
3 sheets
Sheet 1 Sheet 2 Sheet 3
Every citation, both ways
| Document | Relation | Office | Cited during |
|---|---|---|---|
| EP1880718A1 | Cited by | European Patent Office (EPO) | Search report |
| US8221787B2 | Cited by | United States of America | Applicant |
| EP0908177A1 | Cited by | European Patent Office (EPO) | Search report |
| US8298581B2 | Cited by | United States of America | Applicant |
| US5536505A | Cited by | United States of America | Search report |
| EA016683B1 | Cited by | Eurasian Patent Organization (EAPO) | Search report |
| WO0154671A1 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| US9707179B2 | Cited by | United States of America | Applicant |
| US5523095A | Cited by | United States of America | Search report |
| US8617605B2 | Cited by | United States of America | Applicant |
| US9642809B2 | Cited by | United States of America | Applicant |
| WO9220326A1 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| WO2008006506A1 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| US7883722B2 | Cited by | United States of America | Applicant |
| US8449914B2 | Cited by | United States of America | Applicant |
| US7220430B2 | Cited by | United States of America | Applicant |
| US9694080B2 | Cited by | United States of America | Applicant |
| WO2004112746A1 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| EP1095651A2 | Cited by | European Patent Office (EPO) | Search report |
| US8609143B2 | Cited by | United States of America | Applicant |
| EP1095651A3 | Cited by | European Patent Office (EPO) | Search report |
| US9884029B2 | Cited by | United States of America | Applicant |
| EP0072021B1 | Cites | European Patent Office (EPO) | Opposition |
| EP0080341A2 | Cites | European Patent Office (EPO) | Opposition |
| GB2025227A | Cites | United Kingdom | Opposition |
| DE4148802A1 | Cites | Germany | Opposition |
| US4361546A | Cites | United States of America | Opposition |
| US4578264A | Cites | United States of America | Opposition |
| US4610870A | Cites | United States of America | Search report |
| US5068112A | Cites | United States of America | Opposition |
| US5254347A | Cites | United States of America | Opposition |
| CH573749A5 | Cites | Switzerland | Opposition |
| JPS5989622A | Cites | Japan | Opposition |
46 members in 22 offices
Priority claims5
| Document | Office | Kind | Date |
|---|---|---|---|
| 8060488 | Japan | – | |
| 8060488 | Japan | A | |
| 8060488 | Japan | A | |
| 8060488 | – | – | – |
| JP19880080604 | – | – | – |
Members46
| Document | Office | Kind | |
|---|---|---|---|
| FI891163A0 | Finland | A0 | |
| NO891052D0 | Norway | D0 | |
| DK156289D0 | Denmark | D0 | |
| IL89695A0 | Israel | A0 | |
| IL89695D0 | Israel | D0 | |
| IE891006L | Ireland | L | |
| DK156289A | Denmark | A | |
| FI891163A | Finland | A | |
| FI891163L | Finland | L | |
| NO891052L | Norway | L | |
| EP0335560A2This record | European Patent Office (EPO) | A2 | |
| AU3227389A | Australia | A | |
| FR2629344A1 | France | A1 | |
| KR890014095A | Republic of Korea | A | |
| PT90153A | Portugal | A | |
| ZA892131B | South Africa | B | |
| HUT50050A | Hungary | A | |
| JPH021405A | Japan | A | |
| EP0335560A3 | European Patent Office (EPO) | A3 | |
| HU201882B | Hungary | B | |
| AU610711B2 | Australia | B2 | |
| PH25791A | Philippines | A | |
| US5068112A | United States of America | A | |
| BG50712A3 | Bulgaria | A3 | |
| EP0335560B1 | European Patent Office (EPO) | B1 | |
| AT91888T | Austria | T | |
| ATE91888T1 | Austria | T1 | |
| RU1836083C | Russian Federation | C | |
| DE68907762D1 | Germany | D1 | |
| US5254347A | United States of America | A | |
| DE68907762T2 | Germany | T2 | |
| PT90153B | Portugal | B | |
| FR2629344B1 | France | B1 | |
| ES2059729T3 | Spain | T3 | |
| HK76195A | Hong Kong, China | A | |
| KR950007202B1 | Republic of Korea | B1 | |
| IE64348B1 | Ireland | B1 | |
| JPH0791184B2 | Japan | B2 | |
| NO178136B | Norway | B | |
| NO178136C | Norway | C | |
| CA1339078C | Canada | C | |
| FI101344B | Finland | B | |
| FI101344B1 | Finland | B1 | |
| EP0335560B2 | European Patent Office (EPO) | B2 | |
| ES2059729T5 | Spain | T5 | |
| DE68907762T3 | Germany | T3 |
70 legal events, as 5 offices reported them to INPADOC
Over the term
Point at a mark for the eventEvents
| Event | Code | Office | |
|---|---|---|---|
| Be: lapsedLapsedBERE | BERE | EP | |
| Announcement of lapse in spainLapsedFD2A | FD2A | ES | |
| Nl: lapsed or anulled due to non-payment of the annual feeLapsedNLV4 | NLV4 | EP | |
| Gb: european patent ceased through non-payment of renewal feeCeasedGBPC | GBPC | EP | |
| Patent ceasedCeasedPL | PL | CH | |
| Se: european patent has lapsedLapsedEUG | EUG | EP | |
| Appeal reference modifiedAppealORIGINAL CODE: EPIDOSCREFNOAPAH | APAH | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Be: lapsedLapsedBERE | BERE | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Nl: receipt of modified translations in the netherlands language after an opposition procedureOppositionNLR3 | NLR3 | EP | |
| Fr: translation not filedEN | EN | EP | |
| Patent modifiedDC2A | DC2A | ES | |
| Ep patent validated in greeceEP | EP | GR | |
| Nl: receipt of modified translations in the netherlands language after an opposition procedureOppositionNLR3 | NLR3 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Nl: decision of oppositionOppositionNLR2 | NLR2 | EP | |
| Scope or validity of the patent modifiedMAINTIEN DU BREVET DONT L'ETENDUE A ETE MODIFIEEAEN | AEN | CH | |
| Patent maintained in amended form27A | 27A | EP | |
| Designated contracting statesAK | AK | EP | |
| European patent in force as of 2002-01-01IF02 | IF02 | GB | |
| Patent maintained in amended formORIGINAL CODE: 0009272PUAH | PUAH | EP | |
| Information on the status of an ep patent application or granted ep patentGrantedSTATUS: PATENT MAINTAINED AS AMENDEDSTAA | STAA | EP | |
| Interlocutory decision in oppositionOppositionORIGINAL CODE: EPIDOS IDOPPLAW | PLAW | EP | |
| Interlocutory decision in oppositionOppositionORIGINAL CODE: EPIDOS IDOPPLAW | PLAW | EP | |
| Appeal dossier modifiedAppealORIGINAL CODE: EPIDOS NOAPOAPAC | APAC | EP | |
| Appeal dossier modifiedAppealORIGINAL CODE: EPIDOS NOAPOAPAC | APAC | EP | |
| Appeal dossier modifiedAppealORIGINAL CODE: EPIDOS NOAPOAPAC | APAC | EP | |
| Appeal reference modifiedAppealORIGINAL CODE: EPIDOS REFNOAPAE | APAE | EP | |
| Appeal dossier modifiedAppealORIGINAL CODE: EPIDOS NOAPOAPAC | APAC | EP | |
| Se: european patent in force in swedenEAL | EAL | EP | |
| Definitive protectionFG2A | FG2A | ES | |
| Nl: opposition has been filed with the epoOppositionNLR1 | NLR1 | EP | |
| Nl: opposition has been filed with the epoOppositionNLR1 | NLR1 | EP | |
| Opposition filedOpposition26 | 26 | EP | |
| Opposition filedOpposition26 | 26 | EP | |
| Lu: last paid annual feeEPTA | EPTA | EP | |
| Opposition filedOppositionORIGINAL CODE: 0009260PLBI | PLBI | EP | |
| Validation in greece3008940FG4A | FG4A | GR | |
| Corresponds to:REF | REF | EP | |
| Designated contracting statesAK | AK | EP | |
| Corresponds to:REF | REF | EP | |
| (expected) grantORIGINAL CODE: 0009210GRAA | GRAA | EP | |
| It: translation for a ep patent filedITF | ITF | EP | |
| It: translation for a ep patent filedITF | ITF | EP | |
| First examination report despatched17Q | 17Q | EP | |
| Request for examination filed17P | 17P | EP | |
| Designated contracting statesAK | AK | EP | |
| Search report despatchedORIGINAL CODE: 0009013PUAL | PUAL | EP | |
| Designated contracting statesAK | AK | EP | |
| Public reference made under article 153(3) epc to a published international application that has entered the european phaseORIGINAL CODE: 0009012PUAI | PUAI | EP |
Numbers
- Publication
- 0335560
- Publication, DOCDB
- 0335560
- Publication, EPODOC
- EP0335560
- Application
- 89302767
- Application, DOCDB
- 89302767
- Application, EPODOC
- EP19890302767
Titles6
- German
- Arzneizubereitung mit gesteuerter Wirkstofffreisetzung und Verfahren zu deren Herstellung
- English
- Controlled release pharmaceutical preparation and method for producing the same
- French
- Composition pharmaceutique à libération contrôlée et procédé pour sa préparation
- German
- Arzneizubereitung mit gesteuerter Wirkstofffreisetzung und Verfahren zu deren Herstellung.
- English
- Controlled release pharmaceutical preparation and method for producing the same.
- French
- Composition pharmaceutique à libération contrÔlée et procédé pour sa préparation.
Classification
- CPC, 3
- A61K9/5078
- A61K9/16
- A61K9/2866
- IPC, 6
- A61K9 22
- A61K9 28
- A61K9 32
- A61K9 36
- A61K9 50
- A61K9 52
Designated states12
- Contracting states, 12
- Austria
- Belgium
- Switzerland
- Germany
- Spain
- United Kingdom
- Greece
- Italy
- Liechtenstein
- Luxembourg
- Netherlands (Kingdom of the)
- Sweden