CN110237261A - A kind of compound disintegrating agent and preparation method thereof - Google Patents

A kind of compound disintegrating agent and preparation method thereof Download PDF

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Publication number
CN110237261A
CN110237261A CN201910692741.3A CN201910692741A CN110237261A CN 110237261 A CN110237261 A CN 110237261A CN 201910692741 A CN201910692741 A CN 201910692741A CN 110237261 A CN110237261 A CN 110237261A
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China
Prior art keywords
disintegrating agent
compound disintegrating
preparation
compound
agent according
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Pending
Application number
CN201910692741.3A
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Chinese (zh)
Inventor
段民英
杨登科
李洪文
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Zhuhai Dongchen Pharmaceutical Co Ltd
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Zhuhai Dongchen Pharmaceutical Co Ltd
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Priority to CN201910692741.3A priority Critical patent/CN110237261A/en
Publication of CN110237261A publication Critical patent/CN110237261A/en
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/02Inorganic compounds
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/06Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite
    • A61K47/08Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite containing oxygen, e.g. ethers, acetals, ketones, quinones, aldehydes, peroxides
    • A61K47/10Alcohols; Phenols; Salts thereof, e.g. glycerol; Polyethylene glycols [PEG]; Poloxamers; PEG/POE alkyl ethers
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/06Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite
    • A61K47/26Carbohydrates, e.g. sugar alcohols, amino sugars, nucleic acids, mono-, di- or oligo-saccharides; Derivatives thereof, e.g. polysorbates, sorbitan fatty acid esters or glycyrrhizin
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/30Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
    • A61K47/32Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. carbomers, poly(meth)acrylates, or polyvinyl pyrrolidone
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/30Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
    • A61K47/36Polysaccharides; Derivatives thereof, e.g. gums, starch, alginate, dextrin, hyaluronic acid, chitosan, inulin, agar or pectin
    • A61K47/38Cellulose; Derivatives thereof
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2022Organic macromolecular compounds
    • A61K9/205Polysaccharides, e.g. alginate, gums; Cyclodextrin
    • A61K9/2054Cellulose; Cellulose derivatives, e.g. hydroxypropyl methylcellulose

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  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Veterinary Medicine (AREA)
  • Epidemiology (AREA)
  • Medicinal Chemistry (AREA)
  • Animal Behavior & Ethology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Public Health (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Biochemistry (AREA)
  • Molecular Biology (AREA)
  • Medicinal Preparation (AREA)

Abstract

The present invention relates to a kind of compound disintegrating agents and preparation method thereof, the component of compound disintegrating agent includes microcrystalline cellulose, mannitol, xylitol, calcium phosphate dibasic anhydrous, crospovidone, the above component is mixed by weight percentage, compound disintegrating agent is obtained by mixed pulp and spray drying, compound disintegrating agent provided by the invention is low by such environmental effects, disintegrating procedue more rapidly, thoroughly, meets the needs of market.

Description

A kind of compound disintegrating agent and preparation method thereof
Technical field
The present invention relates to drug auxiliary material fields, and in particular to a kind of compound disintegrating agent and preparation method thereof.
Background technique
In modern medicine, disintegrating agent is component part important in preparation, and wherein the quality and performance of disintegrating agent are to medicine Quality plays the role of very important, the basis of the development of disintegrating agent even more preparation and dosage form development.
Disintegrating agent mainly applies to oral drug preparation, as in tablet, granule, capsule and Chinese patent drug pill, Powder etc., main function mechanism be so that preparation is split the substance for being broken into fine particle rapidly in gastro-intestinal Fluid, thus make function at Divide and dissolve and absorb rapidly, then through blood loop distribution at each position of body, scientific selection disintegrating agent is effective ingredient quilt The premise reasonably absorbed, if the disintegrating property of preparation of traditional Chinese medicine composition is poor, the active constituent of drug cannot disappear Change and effectively dissolved out in organ, to reduce the absorbent properties of effective component.
The disintegration ability of preparation of traditional Chinese medicine also suffers from such environmental effects, such as pH value, viscosity, tablet pressure, tablet Hardness, so selecting one kind low by such environmental effects, more rapidly, thoroughly disintegrating agent is particularly important for disintegrating procedue.
Summary of the invention
In view of this, the present invention provide it is a kind of low by such environmental effects, disintegrating procedue more rapidly, thorough disintegrating agent, And the preparation method of the disintegrating agent.
Technical scheme is as follows:
A kind of compound disintegrating agent, including following components in percentage by weight: microcrystalline cellulose 18%~23%, mannitol 55%~65%, xylitol 4%~8%, calcium phosphate dibasic anhydrous 4%~8%, crospovidone 6%~12%.
In one embodiment, the degree of polymerization of microcrystalline cellulose is 155-220;The average grain diameter of calcium phosphate dibasic anhydrous is 30 μm~90 μm;The average grain diameter of crospovidone is 3 μm~30 μm.
Above-mentioned compound disintegrating agent, preparation method are as follows:
A. mixed pulp: the group of above-mentioned weight percent being placed in and is beaten in tank, is added water, control revolving speed 200~ It 500 revs/min, is beaten and slurry is made;
B. be spray-dried: by slurry spray injection drying tower obtained by step a, control inlet air temperature is at 150-300 DEG C, outlet air For temperature at 60~150 DEG C, material pump frequency is 20~50Hz, and atomizer frequency is 20~50Hz, and compound disintegrating agent is made.
In one embodiment, step a is calculated by 35%~55% solid content and water is added, and the concentration of the slurry is 35% ~48%.
In one embodiment, the beating time of step a is 1~3 hour.
In one embodiment, the revolving speed that step a is beaten tank is preferably 255~475 revs/min.
In one embodiment, the inlet air temperature of step b spray drying tower is preferably 170~230 DEG C, and leaving air temp is preferred It is 85~115 DEG C.
In one embodiment, step b expects that pump frequency is preferably 25-47HZ, and atomizer frequency is preferably 28-42HZ.
In one embodiment, the compound disintegrating agent as made from above scheme, size distribution D10:15-35um, D50: 85-125um, D90:180-300um, bulk density 0.40-0.48g/cm3, plain piece, the plain piece suppressed with this compound disintegrating agent Hardness 7-15kg, disintegration time limited are 33 seconds to 64 seconds.
Above-mentioned technical proposal has the following beneficial effects:
1. the degree of polymerization of microcrystalline cellulose and the proportion of microcrystalline cellulose, the partial size of anhydrous phosphoric acid light calcium, crospovidone Distribution is all to influence the principal element of compound disintegrating agent disintegration effect;The microcrystalline cellulose for the use of the degree of polymerization being 155-220, it is average The anhydrous calcium phosphate that partial size is 30 μm~90 μm, the crospovidone that average grain diameter is 3 μm~30 μm, can make compound disintegrating agent Disintegration effect reaches best.
2. by suitably being matched between microcrystalline cellulose and mannitol, xylitol, crospovidone, calcium phosphate dibasic anhydrous Manufactured compound disintegrating agent has good mouthfeel, low in hygroscopicity, by environmental factor (such as pH value, viscosity, tablet pressure, tablet Hardness) influence extremely low effect.
3. calculating when slurrying by 35%-55% solid content and water being added, slurry will not be too dilute or too thick, makes to gather around when spray drying There is good granulating effect, obtains uniform product.
Specific embodiment
For the ease of the understanding of those skilled in the art, below with reference to embodiment, the present invention is further illustrated, real The content for applying example is not limitation of the invention.
Embodiment 1
A kind of compound disintegrating agent, including following components in percentage by weight:
Microcrystalline cellulose 22%, mannitol 62%, xylitol 4%, calcium phosphate dibasic anhydrous 4%, crospovidone 8%;
Wherein:
Microcrystalline cellulose: the degree of polymerization 195,
Mannitol: content 98%-102% pharmaceutical grade
Xylitol: content 98.5%-101% food grade
Calcium phosphate dibasic anhydrous;Density 0.81g/cm3, average grain diameter: 50 μm
Crospovidone: 30 μm of average grain diameter.
Embodiment 2
A kind of compound disintegrating agent, including following components in percentage by weight:
Microcrystalline cellulose 21%, mannitol 63%, xylitol 3%, calcium phosphate dibasic anhydrous 3%, crospovidone 10%;
Wherein:
Microcrystalline cellulose: the degree of polymerization 200,
Mannitol: content 98%-102% pharmaceutical grade
Xylitol: content 98.5%-101% food grade
Calcium phosphate dibasic anhydrous;Density 1.30g/cm3, average grain diameter: 70 μm
Crospovidone: 20 μm of average grain diameter.
Preparation method includes the following steps:
A. mixed pulp: compounding ingredients being placed in by weight percentage in mashing tank, calculates addition water by 45% solid content, Revolving speed is controlled at 280 revs/min, is beaten 1 hour, the slurry that concentration is 45% is made;
B. be spray-dried: by slurry spray injection drying tower obtained by step a, control inlet air temperature is at 200 DEG C, leaving air temp At 95 DEG C, material pump frequency is 30Hz, and atomizer frequency is 32Hz.
Size distribution D10:15um, D50:95um, D90:190um of compound disintegrating agent obtained, bulk density are 0.42g/cm3, disintegration time limited is 38 seconds.
Wherein:
Size distribution is detected using 3000 type laser granulometry of Malvern
Bulk density detection method:
1. above-mentioned microcrystalline cellulose powder about 25mL is taken to be added in dry 50mL graduated cylinder;
2. rotating graduated cylinder, powder is made to sink naturally, top is in a horizontal state, and reads powder volume V;
3. powder is all poured out and weighs weight m, bulk density=m/V.
Disintegration time limited detection method:
1. suitable 0.1mol/l hydrochloric acid solution is added into disintegration tester beaker, into beaker solution temperature reach 37 Degree;
2. the tablet being pressed into compound disintegrating agent is put into the sample cell of bracketplant, baffle is not added, opens lifting motor, Move up and down hanging basket, timing;
3. after the disintegration of tablet in hanging basket all by the mesh screen of tube bottom when, then read access time, each pipe it is initial when Between with disintegration time limited for after disintegration of tablet all by the time difference of mesh screen being the tablet.
Embodiment 3
A kind of compound disintegrating agent, including following components in percentage by weight:
Microcrystalline cellulose 20%, mannitol 60%, xylitol 5%, calcium phosphate dibasic anhydrous 5%, crospovidone 10%;
Wherein:
Microcrystalline cellulose: the degree of polymerization 210
Mannitol: content 98%-102% pharmaceutical grade
Xylitol: content 98.5%-101% food grade
Calcium phosphate dibasic anhydrous;Density 1.33g/cm3Average grain diameter: 60 μm
Crospovidone: average grain diameter: 15 μm.
Preparation method includes the following steps:
A. mixed pulp: compounding ingredients being placed in by weight percentage in mashing tank, calculates addition water by 45% solid content, Revolving speed is controlled at 300 revs/min, is beaten 2 hours, the slurry that concentration is 40% is made;
B. be spray-dried: by slurry spray injection drying tower obtained by step a, control inlet air temperature is at 230 DEG C, leaving air temp At 110 DEG C, material pump frequency is 40HZ, and atomizer frequency is 39HZ.
D10:30 μm of the size distribution of compound disintegrating agent obtained, D50:100 μm, D90:210 μm, bulk density are 0.45g/cm3, disintegration time limited is 36 seconds.
Wherein:
Size distribution is detected using 3000 type laser granulometry of Malvern
Bulk density detection method:
1. above-mentioned microcrystalline cellulose powder about 25mL is taken to be added in dry 50mL graduated cylinder;
2. rotating graduated cylinder, powder is made to sink naturally, top is in a horizontal state, and reads powder volume V;
3. powder is all poured out and weighs weight m, bulk density=m/V.
Disintegration time limited detection method:
1. suitable 0.1mol/l hydrochloric acid solution is added into disintegration tester beaker, into beaker solution temperature reach 37 Degree;
2. the tablet being pressed into compound disintegrating agent is put into the sample cell of bracketplant, baffle is not added, opens lifting motor, Move up and down hanging basket, timing;
3. after the disintegration of tablet in hanging basket all by the mesh screen of tube bottom when, then read access time, each pipe it is initial when Between with disintegration time limited for after disintegration of tablet all by the time difference of mesh screen being the tablet.
Above-described embodiment is the preferable implementation of the present invention, and in addition to this, the present invention can be existing with other way, not Be detached from present inventive concept under the premise of it is any obviously replace it is within the scope of the present invention.

Claims (9)

1. a kind of compound disintegrating agent, which is characterized in that including following components in percentage by weight: microcrystalline cellulose 18%~ 23%, mannitol 55%~65%, xylitol 4%~8%, calcium phosphate dibasic anhydrous 4%~8%, crospovidone 6%~ 12%.
2. compound disintegrating agent as described in claim 1, it is characterised in that the degree of polymerization of the microcrystalline cellulose is 155~220;Nothing The average grain diameter of water calcium monohydrogen phosphate is 30 μm~90 μm;The average grain diameter of crospovidone is 3 μm~30 μm.
3. compound disintegrating agent as described in claim 1, preparation method are as follows:
A. mixed pulp: the group of above-mentioned weight percent being placed in and is beaten in tank, and water is added, and controls revolving speed 200~500 Rev/min, it is beaten and slurry is made;
B. it is spray-dried: by slurry spray injection drying tower obtained by step a, controlling inlet air temperature at 150~300 DEG C, out wind-warm syndrome For degree at 60~150 DEG C, material pump frequency is 20~50Hz, and atomizer frequency is 20~50Hz, and compound disintegrating agent is made.
4. the preparation method of compound disintegrating agent according to claim 3, which is characterized in that solid by 35%~55% in step a Content, which calculates, is added water, and the concentration of the slurry is 35~48%.
5. the preparation method of compound disintegrating agent according to claim 3, which is characterized in that in step a, beating time is 1~3 Hour.
6. the preparation method of compound disintegrating agent according to claim 3, which is characterized in that in step a, the revolving speed for being beaten tank is 255~475 revs/min.
7. the preparation method of compound disintegrating agent according to claim 3, which is characterized in that in step b, spray drying tower into Air temperature is 170~230 DEG C, and leaving air temp is 85~115 DEG C.
8. the preparation method of compound disintegrating agent according to claim 3, which is characterized in that in step b, material pump frequency be 25~ 47 Hz, atomizer frequency are 28~42 Hz.
9. compound disintegrating agent according to claim 1, which is characterized in that size distribution D10 is 15~35um, D50 be 85~ 125um, D90 are 180~300um, and bulk density is 0.4~0.48g/cm3, disintegration time limited is 33 seconds to 64 seconds.
CN201910692741.3A 2019-07-30 2019-07-30 A kind of compound disintegrating agent and preparation method thereof Pending CN110237261A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2595203A (en) * 2020-03-03 2021-11-24 Alkaloid Ad Skopje Formulation
CN113876961A (en) * 2021-09-28 2022-01-04 珠海市东辰制药有限公司 Co-processing auxiliary material and preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1523974A1 (en) * 2003-10-15 2005-04-20 Fuji Chemical Industry Co., Ltd. Composition for rapid disintegrating tablet in oral cavity
US20100216885A1 (en) * 2007-10-30 2010-08-26 Catherine Kabaradjian Orodispersible composition comprising polyunsaturated fatty acids without bad odor or taste
CN101829332A (en) * 2010-05-27 2010-09-15 上海华茂药业有限公司 Rapidly disintegrable pharmaceutic adjuvant and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1523974A1 (en) * 2003-10-15 2005-04-20 Fuji Chemical Industry Co., Ltd. Composition for rapid disintegrating tablet in oral cavity
US20100216885A1 (en) * 2007-10-30 2010-08-26 Catherine Kabaradjian Orodispersible composition comprising polyunsaturated fatty acids without bad odor or taste
CN101829332A (en) * 2010-05-27 2010-09-15 上海华茂药业有限公司 Rapidly disintegrable pharmaceutic adjuvant and preparation method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2595203A (en) * 2020-03-03 2021-11-24 Alkaloid Ad Skopje Formulation
CN113876961A (en) * 2021-09-28 2022-01-04 珠海市东辰制药有限公司 Co-processing auxiliary material and preparation method and application thereof
CN113876961B (en) * 2021-09-28 2024-01-30 珠海市东辰制药有限公司 Co-processing auxiliary material and preparation method and application thereof

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Application publication date: 20190917

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