![]() Compound for incapsulation of biologically active substance
专利摘要:
Composition pour l'enrobage d'une substance biologiquement active qui est stable dans un milieu dont le pH est supérieur ou égal à 5 et qui permet la libération de la substance active dont le pH est inférieur ou égal à 3,5 constituée d'un copolymère aminé basique (copolymère vinylpyridine-styrène) et d'une substance hydrophobe dont le point de fusion est supérieur à 60°C (acide stéarique), la teneur en substance hydrophobe étant comprise entre 50 et 90% de la masse totale de l'enrobage, ainsi que les granulés constitués d'un noyau contenant la substance biologiquement active enrobé par cette composition. 公开号:SU1748630A3 申请号:SU4203248 申请日:1987-09-03 公开日:1992-07-15 发明作者:Ардейон Пьер;Отан Пьер;Буррен Поль;Картиллье Андре 申请人:Рон-Пуленк Санте (Фирма); IPC主号:
专利说明:
" Yo . FIELD: feed production. The purpose of the invention is to increase the stability of the composition at a pH equal to or higher than 5 and release of the biologically active substance at a pH of less than 3.5 while reducing the toxicity of the composition. Example 1. A fluidized bed method in a tank equipped with a WURSTER system is coated with 350 g methionine, pre-granulated in the form of spherical particles, with a content of 98%, the average diameter of which is 0.5-0.63 mm, with a solution having the following composition: Stearic acid (11.1gp. 68 - 69 ° С, acid number 19 198) 88 g Copolymer of 2-vinylpyridine a-styrene (70 - 80) 22 g Copolymer of 2-1,2-dichloroethane 500 cm3 Ethanol500 cm3 Antistatic (Labrazol, registered trademark GAHHEFO SSE) 3 cm3 The viscosity of the 2-vinylpyridine-styrene copolymer (70-80) is 0.5 W (measured at a concentration of 5 g / L in dimethylformamide at 20 ° C). The solution maintained at 27 ° C is sprayed for 3 hours AO minutes. 392 g of coated granules with 73% methionine are obtained. Salting out methionine is determined by dispersing 8 g of the resulting Pu2 00 about 00 about with 3 the granules in 1 liter of the buffer solution maintained at 40 ° C and stirred with a magnetic stirrer. Salted amount of methionine is monitored at sampling, the experiments are carried out at pH 6 and 2. The results are summarized in table 1. „ Example 2 p. 2. Work as in Example 1, but spraying the composition of 1 h 30 min. Get 450 granules with a methionine content of 71.6% The results of the salting out experiments are shown in Table 1, EXAMPLE 3 Example 1 is employed, but a coating composition containing 48.8 g of stearic acid and 12.2 g of 2-vinylpyridine-styrene copolymer (70-30) is used, and spraying occurs. for 1 h at 47 ° C Get 400 g of granules with a methionine content of 82% „ The results of the salting out experiments given in table1, Example 4: Work as in Example 1, but using a coating composition containing 40 g of stearic acid and 10 g of 2-vinylpyridine-styrene copolymer (70-30), and spraying for 45 minutes at 45 ° s Obtain 381 g of granules with a methionine content of 86% 0 The results of experiments on salting out are given in table 1. Example 5: Work as in Example 1, but replacing 1,2-dichloroethane. methylene chloride. The solution maintained at 30 ° C is sprayed for 44 minutes. Obtain 448 g of granules with a methionine content of 76.8%, The results of the experiments on salting out are given in table 1, Example 6: Dissolve 88 g of stearic acid (m.p. 66.9 ° C, acid number 199) and 22 g of 2-vinylpyridine-styrene copolymer (70 - 30) in 80 g of methyl isobutyl ketone. This solution is heated to 85 ° C and added in 8 minutes to a solution mixed with a Polytron-type turbine 990 cm3 of water and 4.2 cm3 of 10% sodium (by volume). An emulsion is obtained, liquid and homogeneous at a temperature higher than or equal to 54 ° C. According to the method of a fluidized bed in a tank equipped with a WURSTER system, cover 350 g of methionine preliminarily granulated in the form of spherical particles, with a content of 98%, the average diameter of which is -: 748630 g, I u S „ ten IS 20 25 thirty 35 ,, 40 e) 45 %- 50 | A, (55 -: It is 0.5-0.63 mm, the emulsion obtained above. The emulsion maintained at 64 ° C is sprayed for 69 minutes. Get 434 g of the coated granules with a methionine content of 78%. The results of experiments on salting out are given in table 1. Example 7: Work as in Example 6, but using an emulsion obtained by dispersion at 8 ° C, thief pactw 88 g of stearic acid and 22 g of 2-vinylpyridine-styrene copolymer (70-30) in 80 g of methyl isobutyl ketone in 495 cm3 of water and 4.2 cm3 of 10% (by volume) sodium. The emulsion, maintained at 66 ° C, is sprayed for 33 minutes. 440 g of coated granules with a methionine content of 77.8% are obtained. The results of experiments on salting out are given in table 1. Example Work according to Example 6, replacing 80 g of methyl isobutyl ketone with 80 g of butyl acetate. The emulsion, maintained at 63 ° C, is sprayed for 65 minutes. 436 g of coated granules with a methionine content of 79% are obtained. The results of experiments on salting out are given in table 1. Example 9: Work as in Example 1, but replacing 350 g of methionine with lysine hydrochloride, previously granulated in the form of spherical particles, the average diameter of which is 0.63 - 0.80 mm and a titer of 82%. - Spray time 3 h 30 min at 27 - 30 ° C. Obtain 450 g of granules containing 60.0% lysine hydrochloride. The results of experiments on salting out are given in table 2. Example 10: Work as in Example 9, but using a coating composition containing 93.5 g of stearic acid and 16.5 g of 2-vinylpyridine-styrene copolymer (70-30), and spraying for 3 hours. 16 min at 28 - 30 ° C. Obtain 380 g of granules containing lysine hydrochloride. The results of experiments on salting out are given in table 2. Example 11: Work as in Example 9, but using a coating composition containing 99 g of stearic acid and 11 g of 2-vinyl copolymer pyridine styrene (70 - 30), and sprayed for 3 hours and 15 minutes at 29 - 35 ° C. Get g granules with a content of 60.2% lysine hydrochloride „ The results of the salting out experiments are given in Table 2 Example 12: Work as in Example 9, but using a coating composition containing 77 g of stearic acid and 33 g of 2-vinylpyridine-styrene copolymer (70-30), and spraying for 1 h 50 min at 32 -. Get A60 g of granules with lysine hydrochloride content of 58, H%. The results of the salting out experiments are given in .2. Example 13: Work as in Example 9, but using a coating composition containing 60.5 g of stearic acid and A3.5 g of 2-vinylpyridine-styrene copolymer (70-30), and spraying for 2 hours. 10 min at 39 - 1 ° С. Get 60 g of granules with a content of lysine hydrochloride of 59.8%. The results of the salting out experiments are given in Table 2. PRI me R I. Work as in Example 9, but spraying is carried out for 1 h 30 min at 37 - 39 ° C. Part 55 g of granules with a lysine chlorohydrate content of 61% is obtained. The results of experiments on salting out are given in table 2. Example 15: Work as in Example 9, but using a solution of the composition for coating in pure tetrahydrofuran and spraying for 2 hours at 20 ° C. 57 g of granules with a lysine hydrochloride content of 60.7% are obtained. The results of experiments on salting out are given in table 3. Example 16: Work as in Example 9, but using a solution of the composition for coating in a mixture of ethanol - tetrahydrofuran 1-1 (by volume) and spraying for 1 hour kQ min at 20 ° C. 57 g of granules with a lysine hlrhydrate content are obtained. 62%. The results of experiments on salting out are listed in Table 2. Example 17: Work at stage 9, but using a solution of the composition for coating in a mixture of ethanol 8630 acetone 1-1 (by volume) and sprayed for 3 hours and 30 minutes at r40 ° C. 455 g of granules are obtained with a lysine hydrochloride content of 59.2%. The results of experiments on salting out are given in table 2. Example 18. Work as in example 9, but using a composition for JQ coating, not containing antistatic The solution maintained at 35 ° C is sprayed for 1 hour and 0 minutes. 56 g of coated granules with co. holding lysine hydrochloride 60%. jj - the results of experiments on salting out are given in table 2. Example 19: Work as in Example 9, but using a coating solution in which 1,2-dichloroethane 20 is replaced with the same amount of chloro-. that methylene. The solution maintained at 35 ° C is sprayed for 2 minutes. 55 g of coated granules with a content of 25 to 59% lysine hydrochloride are obtained. The results of experiments on salting out are given in table 2. EXAMPLE 20 This emulsion prepared according to Example 6 is used to coat 350 g of lysine hydrochloride, previously granulated in the form of spherical particles, the average diameter of which is 0.6335 0.80 mm with a titer of 82%. The emulsion maintained at 65 ° C is sprayed for 6 hours. 51 g of coated granules are obtained with a lysine chlorohydrate content of 57%. 40 The results of the salting out experiments are given in table 2, The efficacy in vivo of the proposed formulations for coating 45 can be shown as follows. test, v Samples of coated granules (approximately 0.5 g) are introduced into 6 packets of 0 nylon, having a mesh of 300 300 microns. The bags are placed on h8 h in the hem of the fatigue sheep. The bags are then removed and washed. One product is used for 3 or k sheep. The amount of active substance contained in the packets is determined by an appropriate method. The results are shown in Table 3. 32.2 M), 9 9.2 6.6 11.1 having 114.8 g 28.7 g 650 cm3 650 cm3 71 EXAMPLE 23: By the Spray coating method, 350 g of granules containing vitamin A acetate, the diameter of which is 0.5-0.8 mm, are coated and have the following composition, in wt.%: Vitamin A Acetate Gelatin Laktza Glycemy Stabilizers solution, for coating, the following composition: Stearic acid Copolymer of 2-vinylpyridine-styrene (70 - 30) Ethanol 1,2-dichloroethane The solution maintained at 3 ° C is sprayed at the rate of 10 cm3 / min. Covered granules are obtained, in which the grown titer of vitamin A is 618,000 uJ / r, the starting granules have a titer uJ / r. Salting out in a test tube is determined at 37 ° C in artificial gastric medium at pH 1.2 in the presence of pepsin (by USE XX). After 2 hours, the percentage of salted active substance is 93% for coated granules and 86% for the original granules. eight After 8 hours, the rumen resistance is 96.0 and 3.2% for the coated granules and granules. 3.0 i 2.2% - for initial five 6 S The table shows the number of components in the composition, corresponding to the examples.
权利要求:
Claims (1) [1] Invention Formula A composition for encapsulating a biologically active substance, including an amine-containing polymer and a hydrophobic substance, characterized in that, in order to increase the stability of the composition at pH 5 and release the biologically active substance, pH Ј 3.5 while reducing the toxicity of the composition, The polymer containing the composition contains a copolymer of styrene with 2-vinylpyridine, and as a hydrophobic substance, stearic acid with a melting point of 66.9 - 69 ° C and an acid number of 19 - T99 in the following ratio of components,%: copolymer with Tyrol with 2-vinylpyridine 10.0-5.0; stearic acid with a melting point of 66.9 - 69 ° C and an acid number of 191 - 199 55.0 - 90.0 Table3 eleven Table 12
类似技术:
公开号 | 公开日 | 专利标题 SU1748630A3|1992-07-15|Compound for incapsulation of biologically active substance EP0077264B1|1988-03-23|Composition for coating food and drugs, and granules so coated Teixeira et al.1990|Assessment of chitosan gels for the controlled release of agrochemicals JP3803121B2|2006-08-02|Stable natamycin suspension US4542042A|1985-09-17|Process for preparing free-flowing ethylcellulose microcapsules CH647958A5|1985-02-28|METHOD FOR PRODUCING MICROCAPSULES CONTAINING A PHARMACEUTICALLY ACTIVE COMPOUND. CN1010315B|1990-11-07|Low viscosity heteropolysaccharides EP0193917A2|1986-09-10|Water dispersible and water soluble carbohydrate polymer compositions for parenteral administration FR2586030A1|1987-02-13|GELATIN WITH IMPROVED PROPERTIES AND PROCESS FOR THE PREPARATION THEREOF BY WELDING WITH HYDROLYZED GELATIN AU618096B2|1991-12-12|Controlled release of active ingredients from capsules having a salt sensitive shell material FR2622198A1|1989-04-28|GRANULATED COMPOSITIONS OF INSTANTANEOUS AQUEOUSLY DISSOLVED POLYSACCHARIDES, PROCESS FOR THEIR PREPARATION AND USE CA2044548C|2000-05-16|Coating process by a ph-sensitive polymer of active ingredients CA1160536A|1984-01-17|Concentrated aqueous metal aldonate and/or ammoniumaldonate composition KR910003557B1|1991-06-05|Process for preparing liquid prolonged release pharmaceutical formulations EP0447297A1|1991-09-18|Method for coating active agents with zein US5660769A|1997-08-26|Method of encapsulating substances in biocapsules EP0206890B1|1990-08-29|Product for feeding ruminants and its preparation WO1985003648A1|1985-08-29|Capsules and process for their preparation CA2105793A1|1994-03-12|Process for producing compositions for ruminants EP0293975B1|1991-07-24|Dry, rapidly soluble, compositions of beta-lactam antibiotics US6096345A|2000-08-01|Composition of an active component and free flowing particles of a polysaccharide matrix having significantly improved water dispersibility and stability in aqueous solutions JPH035402A|1991-01-11|Dispersing agent and composition for suspended killing agent JP2004525954A|2004-08-26|Foamable solid composition JPS6439987A|1989-02-10|Comprehensive immobilized organism catalyst EP0653159B1|1999-08-18|Desinfecting composition
同族专利:
公开号 | 公开日 AT72938T|1992-03-15| FR2603458B1|1990-11-02| KR950012885B1|1995-10-23| ES2029483T3|1992-08-16| AU7779487A|1988-03-10| FR2603458A1|1988-03-11| ZA876578B|1988-03-07| DE3777032D1|1992-04-09| KR880003572A|1988-05-28| AR242091A1|1993-03-31| NZ221646A|1991-08-27| HU196310B|1988-11-28| EP0260186A3|1988-12-21| US4877621A|1989-10-31| JP2546852B2|1996-10-23| JPS6363350A|1988-03-19| CA1324958C|1993-12-07| HUT45402A|1988-07-28| EP0260186A2|1988-03-16| AU613873B2|1991-08-15| EP0260186B1|1992-03-04|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 RU2730641C2|2015-12-02|2020-08-24|Пуратос Нв|Encapsulated fillings|US100404A|1870-03-01|Self and j | FR2401620B1|1977-09-02|1983-02-25|Eastman Kodak Co| FR2401619B1|1977-09-02|1983-02-25|Eastman Kodak Co| US4196187A|1977-09-02|1980-04-01|Eastman Kodak Company|Rumen-stable pellets| US4181710A|1977-09-02|1980-01-01|Eastman Kodak Company|Rumen-stable pellets| UST100404I4|1980-02-29|1981-03-03|Rumen-stable pellet coatings| FR2514261B1|1981-10-08|1986-08-22|Aec Chim Organ Biolog|NOVEL COMPOSITION FOR COATING FOODS AND DRUGS AND GRANULES THUS COATED| DE3366815D1|1982-07-12|1986-11-20|Eastman Kodak Co|ROOM STABLE PELLETS| WO1984004657A1|1983-05-26|1984-12-06|Eastman Kodak Co|Rumen-stable pellets| JPS60141243A|1983-12-27|1985-07-26|Nippon Soda Co Ltd|Feed additive composition for ruminant| US4713245A|1984-06-04|1987-12-15|Mitsui Toatsu Chemicals, Incorporated|Granule containing physiologically-active substance, method for preparing same and use thereof| JPS6188844A|1984-10-05|1986-05-07|Kyowa Hakko Kogyo Co Ltd|Feed additive composition for ruminant| US4780315A|1985-11-25|1988-10-25|Eastman Kodak Company|Rumen-stable pellets|FR2648020B1|1989-06-12|1992-03-13|Rhone Poulenc Sante|USE OF COMPOSITIONS DEGRADABLY BY ENZYMATICS FOR THE COATING OF FOOD ADDITIVES FOR RUMINANTS| US5093128A|1989-07-18|1992-03-03|Draguesku Oliver J|Rumen and other stomach chamber bypass nutrients and methods of fabrication| FR2652721B1|1989-10-10|1992-06-19|Rhone Poulenc Nutrition Animal|USE OF CHEESE DAIRY FROM ANIMAL-ACOUSED ANIMALS.| US5225218A|1989-10-10|1993-07-06|Rhone-Poulenc Nutrition Animale|Method of making cheese with milk obtained from animals fed with a feed supplemented with an amino acid| FR2654307B1|1989-11-10|1992-02-21|Rhone Poulenc Nutrition Animal|USE OF PROTEIN AMINO ACIDS FOR SHEEP FEEDING.| FR2659231A1|1990-03-08|1991-09-13|Rhone Poulenc Sante|ZEIN COATING PROCESS OF ACTIVE INGREDIENTS.| FR2659230A1|1990-03-08|1991-09-13|Rhone Poulenc Sante|PROCESS FOR COATING A ACTIVE SENSITIVE PH POLYMER OF ACTIVE INGREDIENTS.| FR2663207B1|1990-06-15|1993-04-30|Rhone Poulenc Nutrition Animal|PROCESS FOR COATING A ACTIVE SENSITIVE PH POLYMER OF ACTIVE INGREDIENTS.| FR2663867B1|1990-06-29|1994-08-05|Rhone Poulenc Nutrition Animal|PROCESS FOR SMOOTHING GRANULES OF ACTIVE INGREDIENTS.| FR2663818B1|1990-06-29|1993-07-09|Rhone Poulenc Nutrition Animale|PROCESS FOR THE PREPARATION OF GRANULES OF ACTIVE PRINCIPLES BY EXTRUSION.| US5292657A|1990-12-31|1994-03-08|Pioneer Hi-Bred International, Inc.|Process for preparing rotary disc fatty acid microspheres of microorganisms| DE4100920C2|1991-01-15|1992-10-08|Degussa Ag, 6000 Frankfurt, De| AU3472193A|1992-03-20|1993-10-21|Church & Dwight Company, Inc.|Encapsulated dietary fatty acid salt products| JP3188767B2|1992-09-11|2001-07-16|協和醗酵工業株式会社|Method for producing a ruminant composition| US5616339A|1992-09-18|1997-04-01|Rhone-Poulenc Nutrition Animale|Chitosan-based nutrient or medicinal compositions for administration to ruminants| FR2695804B1|1992-09-18|1994-11-25|Rhone Poulenc Nutrition Animal|Nutritional or medicinal compositions for administration to ruminants based on chitosan.| CA2140298C|1994-01-14|1998-12-08|Thomas L. Meade|Rumen by-pass feed supplement| FR2719477B1|1994-05-06|1996-06-07|Rhone Poulenc Nutrition Animal|Use of active ingredients protected against degradation in the rumen as hepatoprotectors.| FR2763853B1|1997-05-28|2000-01-07|Oreal|ASSOCIATION OF A RETINOIDE WITH A POLYAMINE POLYMER| DE19962427A1|1999-12-22|2001-07-12|Nutrinova Gmbh|Encapsulated multifunctional, biologically active food component, process for their production and their application| US6685978B1|2000-04-04|2004-02-03|Cp Kelco Aps|Gelled and gellable compositions for food products| EP1177726A1|2000-08-04|2002-02-06|Aventis Animal Nutrition S.A.|Process for the production of granules of methionine| DE10220785A1|2002-05-10|2003-11-20|Degussa|Protected active substance preparations from amino acids and process for their preparation| US20050106250A1|2002-05-10|2005-05-19|Hasseberg Hans A.|Protected active compound formulations of amino acids and process for their preparation| US20070231369A1|2006-03-31|2007-10-04|Rlc Technologies, L.L.C.|Ruminant feed composition and method of making| FR2909685B1|2006-12-08|2012-12-21|Lallemand Sas|ACTIVE DRIED DRIED YEASTS AND FOODS CONTAINING THEM| WO2013113982A1|2012-01-31|2013-08-08|Raisio Plc|Ruminant feed enhancing energy metabolism in milk production|
法律状态:
2005-04-20| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: RH4F Effective date: 20050127 | 2006-11-20| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: PD4A | 2007-02-27| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: PC4A Effective date: 20070119 | 2007-03-20| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: PC4A Effective date: 20070130 |
优先权:
[返回顶部]
申请号 | 申请日 | 专利标题 FR8612412A|FR2603458B1|1986-09-04|1986-09-04|NOVEL COMPOSITIONS FOR COATING FOOD ADDITIVES FOR RUMINANTS AND FOOD ADDITIVES THUS COATED| 相关专利
Sulfonates, polymers, resist compositions and patterning process
Washing machine
Washing machine
Device for fixture finishing and tension adjusting of membrane
Structure for Equipping Band in a Plane Cathode Ray Tube
Process for preparation of 7 alpha-carboxyl 9, 11-epoxy steroids and intermediates useful therein an
国家/地区
|