CN118750458A - A preparation method of simvastatin tablets - Google Patents
A preparation method of simvastatin tablets Download PDFInfo
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- CN118750458A CN118750458A CN202410846801.3A CN202410846801A CN118750458A CN 118750458 A CN118750458 A CN 118750458A CN 202410846801 A CN202410846801 A CN 202410846801A CN 118750458 A CN118750458 A CN 118750458A
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- RYMZZMVNJRMUDD-HGQWONQESA-N simvastatin Chemical compound C([C@H]1[C@@H](C)C=CC2=C[C@H](C)C[C@@H]([C@H]12)OC(=O)C(C)(C)CC)C[C@@H]1C[C@@H](O)CC(=O)O1 RYMZZMVNJRMUDD-HGQWONQESA-N 0.000 title claims abstract description 72
- 229960002855 simvastatin Drugs 0.000 title claims abstract description 72
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
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- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 claims description 32
- 239000008187 granular material Substances 0.000 claims description 27
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- 229920002785 Croscarmellose sodium Polymers 0.000 claims description 8
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 claims description 8
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- 239000000378 calcium silicate Substances 0.000 claims description 8
- 229910052918 calcium silicate Inorganic materials 0.000 claims description 8
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 claims description 8
- 235000010947 crosslinked sodium carboxy methyl cellulose Nutrition 0.000 claims description 8
- 239000008101 lactose Substances 0.000 claims description 8
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- 239000008108 microcrystalline cellulose Substances 0.000 claims description 8
- 229940016286 microcrystalline cellulose Drugs 0.000 claims description 8
- 229920002472 Starch Polymers 0.000 claims description 7
- GUBGYTABKSRVRQ-QUYVBRFLSA-N beta-maltose Chemical compound OC[C@H]1O[C@H](O[C@H]2[C@H](O)[C@@H](O)[C@H](O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@@H]1O GUBGYTABKSRVRQ-QUYVBRFLSA-N 0.000 claims description 7
- 239000011734 sodium Substances 0.000 claims description 7
- 229910052708 sodium Inorganic materials 0.000 claims description 7
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000011362 coarse particle Substances 0.000 claims description 4
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-Lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 claims description 2
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 claims description 2
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 claims description 2
- MKRNVBXERAPZOP-UHFFFAOYSA-N Starch acetate Chemical compound O1C(CO)C(OC)C(O)C(O)C1OCC1C(OC2C(C(O)C(OC)C(CO)O2)OC(C)=O)C(O)C(O)C(OC2C(OC(C)C(O)C2O)CO)O1 MKRNVBXERAPZOP-UHFFFAOYSA-N 0.000 claims description 2
- 238000007908 dry granulation Methods 0.000 claims description 2
- 238000001125 extrusion Methods 0.000 claims description 2
- 239000010419 fine particle Substances 0.000 claims description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 235000012239 silicon dioxide Nutrition 0.000 claims description 2
- 239000000600 sorbitol Substances 0.000 claims description 2
- 238000007906 compression Methods 0.000 claims 3
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- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims 1
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 claims 1
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 claims 1
- 229960001681 croscarmellose sodium Drugs 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 238000004513 sizing Methods 0.000 claims 1
- 230000004580 weight loss Effects 0.000 claims 1
- 239000003814 drug Substances 0.000 abstract description 9
- 229940079593 drug Drugs 0.000 abstract description 8
- 239000000825 pharmaceutical preparation Substances 0.000 abstract 1
- 239000001767 crosslinked sodium carboxy methyl cellulose Substances 0.000 description 7
- 238000004090 dissolution Methods 0.000 description 7
- 229940032147 starch Drugs 0.000 description 6
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 4
- 238000009835 boiling Methods 0.000 description 3
- 239000012738 dissolution medium Substances 0.000 description 3
- 239000004480 active ingredient Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000008280 blood Substances 0.000 description 2
- 210000004369 blood Anatomy 0.000 description 2
- 235000012000 cholesterol Nutrition 0.000 description 2
- 238000000338 in vitro Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 208000024172 Cardiovascular disease Diseases 0.000 description 1
- 229940121710 HMGCoA reductase inhibitor Drugs 0.000 description 1
- 208000035150 Hypercholesterolemia Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003524 antilipemic agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 208000029078 coronary artery disease Diseases 0.000 description 1
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Classifications
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/20—Pills, tablets, discs, rods
- A61K9/2004—Excipients; Inactive ingredients
- A61K9/2022—Organic macromolecular compounds
- A61K9/205—Polysaccharides, e.g. alginate, gums; Cyclodextrin
- A61K9/2059—Starch, including chemically or physically modified derivatives; Amylose; Amylopectin; Dextrin
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/33—Heterocyclic compounds
- A61K31/335—Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin
- A61K31/365—Lactones
- A61K31/366—Lactones having six-membered rings, e.g. delta-lactones
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P3/00—Drugs for disorders of the metabolism
- A61P3/06—Antihyperlipidemics
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P9/00—Drugs for disorders of the cardiovascular system
- A61P9/10—Drugs for disorders of the cardiovascular system for treating ischaemic or atherosclerotic diseases, e.g. antianginal drugs, coronary vasodilators, drugs for myocardial infarction, retinopathy, cerebrovascula insufficiency, renal arteriosclerosis
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Abstract
本发明涉及一种辛伐他汀片剂的制备方法,属于药物制剂技术领域。提供一种辛伐他汀片剂的制备方法,该方法包括将辛伐他汀进行超声波粉碎,得到辛伐他汀超微粉,将辛伐他汀超微粉与部分预胶化淀粉一同粉碎,过筛,将得到的粉碎混合物与填充剂一起加入干法制粒机中经0.8mm筛网进行制粒,得到辛伐他汀混合物颗粒,喷雾干燥,将得到的颗粒与药用辅料混合,压制成片芯,将所得片芯进行薄膜包衣,得到辛伐他汀片剂;本发明整体上具有药品的质量高、原料微粉损耗较少的优点。
The present invention relates to a preparation method of simvastatin tablets, belonging to the technical field of pharmaceutical preparations. A preparation method of simvastatin tablets is provided, the method comprising ultrasonically grinding simvastatin to obtain simvastatin ultrafine powder, grinding the simvastatin ultrafine powder together with part of pregelatinized starch, sieving, adding the obtained grinding mixture and filler into a dry granulator for granulation through a 0.8mm screen to obtain simvastatin mixture particles, spray drying, mixing the obtained particles with pharmaceutical excipients, pressing into tablet cores, and film coating the obtained tablet cores to obtain simvastatin tablets; the present invention as a whole has the advantages of high drug quality and less loss of raw material micropowder.
Description
技术领域Technical Field
本发明涉及一种辛伐他汀片剂的制备方法,属于药物片剂制备领域。The invention relates to a method for preparing a simvastatin tablet, and belongs to the field of preparation of drug tablets.
背景技术Background Art
辛伐他汀(simvastatin)是他汀类(statin)的降血脂药物,用于控制血液中胆固醇的含量以及预防心血管疾病,可抑制内源性胆固醇的合成,为血酯调节剂,临床用于治疗高胆固醇血症,冠心病。Simvastatin is a lipid-lowering drug of the statin class, used to control the cholesterol content in the blood and prevent cardiovascular diseases. It can inhibit the synthesis of endogenous cholesterol and is a blood lipid regulator. It is clinically used to treat hypercholesterolemia and coronary heart disease.
在辛伐他汀片剂的制备过程中,传统方法通常包括将活性成分与辅料直接混合,然后通过沸腾制粒、压片等步骤完成。然而,由于需要加热,对于热敏感物质可能会有一定的限制,所以沸腾制粒过程中可能引起活性成分的稳定性下降,影响药品的质量;此外,沸腾过程中微粉可能会飞扬造成原料损耗,需要有效的粉尘控制设备,不利于大规模工业化生产。In the preparation process of simvastatin tablets, the traditional method usually includes directly mixing the active ingredient with the excipients, and then completing it through steps such as boiling granulation and tableting. However, due to the need for heating, there may be certain restrictions on heat-sensitive substances, so the boiling granulation process may cause the stability of the active ingredient to decrease, affecting the quality of the drug; in addition, during the boiling process, micropowders may fly and cause raw material loss, requiring effective dust control equipment, which is not conducive to large-scale industrial production.
发明内容Summary of the invention
本发明针对以上现有技术中存在的缺陷,提供一种辛伐他汀片剂的制备方法,解决的问题是提高药品的质量、减少原料微粉损耗的合成方法。The present invention aims at the defects existing in the above prior art and provides a method for preparing simvastatin tablets, which solves the problem of improving the quality of the medicine and reducing the loss of raw material micro powder.
本发明的目的是通过以下技术方案得以实现的,一种辛伐他汀片剂的制备方法,该方法包括:The object of the present invention is achieved by the following technical scheme: a method for preparing simvastatin tablets, the method comprising:
S1:将辛伐他汀进行超声波粉碎,得到辛伐他汀超微粉;S1: subjecting simvastatin to ultrasonic grinding to obtain simvastatin ultrafine powder;
S2:将辛伐他汀超微粉与部分预胶化淀粉一同粉碎,过筛;S2: pulverize simvastatin ultrafine powder and part of pregelatinized starch together and sieve;
S3:将步骤S2得到的粉碎混合物与填充剂一起加入干法制粒机中经0.8mm筛网进行制粒,得到辛伐他汀混合物颗粒,喷雾干燥;S3: adding the crushed mixture obtained in step S2 together with the filler into a dry granulator for granulation through a 0.8 mm sieve to obtain simvastatin mixture particles, and spray drying;
S4:将步骤S3得到的颗粒与药用辅料混合,压制成片芯;S4: mixing the particles obtained in step S3 with pharmaceutical excipients and pressing them into tablet cores;
S5:将步骤S4所得片芯进行薄膜包衣,得到辛伐他汀片剂。S5: Film-coating the tablet core obtained in step S4 to obtain simvastatin tablets.
进一步的,所述步骤S1中,采用超声波粉碎机将辛伐他汀进行振动粉碎,所述辛伐他汀超微粉的比表面积为1900~2050m2/kg。Furthermore, in the step S1, an ultrasonic pulverizer is used to vibrate and pulverize simvastatin, and the specific surface area of the simvastatin ultrafine powder is 1900-2050 m2/kg.
进一步的,所述步骤S2中,采用涡轮自冷式无尘粉碎机进行粉碎,所述过筛所用筛网目数为144~225目。Furthermore, in the step S2, a turbine self-cooling dust-free pulverizer is used for pulverization, and the mesh number of the sieve used for sieving is 144-225 meshes.
采用粉碎可使得辛伐他汀超微粉与预胶化淀粉初步混合,同时起到一个简单的混合的作用,更有利于颗粒的含量均一性。The pulverization can make the simvastatin ultrafine powder and the pregelatinized starch initially mixed, and at the same time play a simple mixing role, which is more conducive to the uniformity of the content of the particles.
进一步的,所述步骤S2中,所述辛伐他汀超微粉与所述部分预胶化淀粉先按照连续混合法进行混合,原料供给速度为6~10kg/min,混合速度为50~200r/min。Furthermore, in step S2, the simvastatin ultrafine powder and the partially pregelatinized starch are first mixed according to a continuous mixing method, with a raw material supply speed of 6-10 kg/min and a mixing speed of 50-200 r/min.
混合过程中原料的供给和混合是连续进行的,适用于需要大规模生产以及连续加工的情况,能够实现高效、持续的混合过程。The supply and mixing of raw materials during the mixing process are carried out continuously, which is suitable for situations requiring large-scale production and continuous processing, and can achieve an efficient and continuous mixing process.
进一步的,所述步骤S3中,干法制粒的步骤包括:Furthermore, in step S3, the step of dry granulation comprises:
T1:将得到的粉碎混合物与填充剂按1:2~5的比例混合均匀,完成混合后输送到干法制粒机内;T1: The obtained pulverized mixture is mixed evenly with the filler in a ratio of 1:2-5, and after the mixing is completed, it is conveyed to the dry granulator;
T2:在干法制粒机内,通过旋转式制粒机、挤压式制粒机等设备利用机械压力将原料压缩成颗粒;T2: In the dry granulator, the raw materials are compressed into granules by mechanical pressure through equipment such as rotary granulators and extrusion granulators;
T3:制粒过程中添加硬脂酸镁提高颗粒的流动性和成形性;T3: magnesium stearate was added during granulation to improve the fluidity and formability of the granules;
T4:制粒完成后,将颗粒输送到干燥设备中进行干燥,干燥温度为45~55℃,所得颗粒的干燥失重≤5.0%。T4: After granulation is completed, the granules are transported to a drying device for drying at a drying temperature of 45-55°C. The drying loss of the obtained granules is ≤5.0%.
作为优选,粉碎混合物与填充剂按1:3的比例混合。Preferably, the crushed mixture and the filler are mixed in a ratio of 1:3.
进一步的,所述步骤S2中,所述填充剂选自山梨醇、麦芽糖、乳糖、交联羧甲基纤维素钠、微晶纤维素、淀粉醋酸酯中的一种或多种。Furthermore, in step S2, the filler is selected from one or more of sorbitol, maltose, lactose, cross-linked sodium carboxymethyl cellulose, microcrystalline cellulose, and starch acetate.
进一步的,所述步骤S3中,所述喷雾干燥之后还包括将颗粒过筛网的步骤,将整好的辛伐他汀混合物颗粒经真空上料机吸入三元旋振筛,利用20目的筛网去粗粒,利用60目的筛网去细粒,粗颗粒重复整粒,收得重粉颗粒。Furthermore, in the step S3, after the spray drying, the particles are also screened, the sized simvastatin mixture particles are sucked into a three-dimensional rotary vibrating screen through a vacuum feeder, a 20-mesh screen is used to remove coarse particles, a 60-mesh screen is used to remove fine particles, and the coarse particles are repeatedly sized to obtain heavy powder particles.
进一步的,所述步骤S3中,干法制粒机的压辊压力为8~10MPa,压辊间隙0.6~0.9mm,压辊转速15~20r/min,三元旋振筛转速为100~120r/min。Furthermore, in step S3, the roller pressure of the dry granulator is 8-10 MPa, the roller gap is 0.6-0.9 mm, the roller speed is 15-20 r/min, and the three-element rotary vibrating screen speed is 100-120 r/min.
进一步的,所述步骤S4中,所述药用辅料包括硬脂酸盐、二氧化硅、麦芽糖、硅酸钙与羧甲淀粉钠中的一种或多种。Furthermore, in step S4, the pharmaceutical excipients include one or more of stearate, silicon dioxide, maltose, calcium silicate and sodium carboxymethyl starch.
一种辛伐他汀片剂,包括的组成成分种类及各组成成分重量配比为:辛伐他汀10~35重量份、部分预胶化淀粉10~15重量份、填充剂20~75重量份、硬脂酸镁3~9重量份、药用辅料10~18重量份。A simvastatin tablet comprises the following components and their weight ratios: 10-35 parts by weight of simvastatin, 10-15 parts by weight of partially pregelatinized starch, 20-75 parts by weight of a filler, 3-9 parts by weight of magnesium stearate and 10-18 parts by weight of a pharmaceutical excipient.
综上所述,本发明与现有技术相比,具有以下优点:In summary, compared with the prior art, the present invention has the following advantages:
1、本发明中,当辛伐他汀被微粉化处理后,粒度和比表面积提高,药物颗粒与溶出介质的接触面积增大,增大的接触面积有利于药物颗粒更快、更完全地溶解在溶出介质中,从而提高体外溶出度,均匀的颗粒大小分布有助于药物在溶出介质中均匀溶解,从而提高溶出度的均匀性,体外溶出度的提高和溶出度均匀性的改善,有利于药物在体内更快、更均匀地释放和吸收;1. In the present invention, after simvastatin is micronized, the particle size and specific surface area are increased, and the contact area between the drug particles and the dissolution medium is increased. The increased contact area is conducive to faster and more complete dissolution of the drug particles in the dissolution medium, thereby improving the in vitro dissolution rate. The uniform particle size distribution helps the drug to dissolve uniformly in the dissolution medium, thereby improving the uniformity of the dissolution rate. The improvement of the in vitro dissolution rate and the improvement of the dissolution uniformity are conducive to faster and more uniform release and absorption of the drug in the body;
2、本发明中,采用超声波粉碎机对辛伐他汀进行振动粉碎,得到比表面积较大的辛伐他汀超微粉,有利于提高药物溶出速度和生物利用度,从而提高疗效,利用涡轮自冷式无尘粉碎机对辛伐他汀超微粉和预胶化淀粉进行粉碎,并通过144目筛,确保了原料的细度和均匀性,有利于提高产品质量;2. In the present invention, an ultrasonic pulverizer is used to vibrate and pulverize simvastatin to obtain simvastatin ultrafine powder with a large specific surface area, which is beneficial to improving the drug dissolution rate and bioavailability, thereby improving the therapeutic effect. A turbine self-cooling dust-free pulverizer is used to pulverize simvastatin ultrafine powder and pregelatinized starch, and the pulverized powder is passed through a 144-mesh sieve, thereby ensuring the fineness and uniformity of the raw materials, which is beneficial to improving the product quality.
3、本发明中,采用干法制剂过程中喷入部分预胶化淀粉,避免了原料微粉飞扬造成原料损耗。3. In the present invention, part of the pregelatinized starch is sprayed in the dry preparation process, thereby avoiding the loss of raw materials caused by the flying of raw material powder.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为本发明的制备流程图;Fig. 1 is a preparation flow chart of the present invention;
图2为本发明的溶出度对比图。FIG. 2 is a dissolution comparison diagram of the present invention.
具体实施方式DETAILED DESCRIPTION
下面通过具体实施例,对本发明的技术方案作进一步具体的说明,但是本发明并不限于这些实施例。The technical solution of the present invention is further specifically described below through specific embodiments, but the present invention is not limited to these embodiments.
按如下份数准备原料:辛伐他汀18重量份、部分预胶化淀粉12重量份、填充剂54重量份(微晶纤维素20重量份、乳糖15重量份、交联羧甲基纤维素钠19重量份)、硬脂酸镁6重量份、药用辅料10重量份 (羧甲淀粉钠5重量份、硬脂酸镁2重量份、麦芽糖1重量份、硅酸钙2重量份)。Prepare the raw materials according to the following amounts: 18 parts by weight of simvastatin, 12 parts by weight of partially pregelatinized starch, 54 parts by weight of filler (20 parts by weight of microcrystalline cellulose, 15 parts by weight of lactose, 19 parts by weight of cross-linked sodium carboxymethyl cellulose), 6 parts by weight of magnesium stearate, and 10 parts by weight of pharmaceutical excipients (5 parts by weight of sodium carboxymethyl starch, 2 parts by weight of magnesium stearate, 1 part by weight of maltose, and 2 parts by weight of calcium silicate).
(1)将辛伐他汀采用超声波粉碎机进行振动粉碎,得到比表面积为2050m2/kg的辛伐他汀超微粉;(1) pulverizing simvastatin by vibration using an ultrasonic pulverizer to obtain simvastatin ultrafine powder with a specific surface area of 2050 m2/kg;
(2)将微粉后辛伐他汀与预胶化淀粉采用涡轮自冷式无尘粉碎机进行粉碎,粉碎后过144目筛,其中,辛伐他汀超微粉与预胶化淀粉先按照连续混合法进行混合后再进行粉碎,原料供给速度为8kg/min,混合速度为125rpm/min;(2) The micronized simvastatin and pregelatinized starch were pulverized by a turbine self-cooling dust-free pulverizer and passed through a 144-mesh sieve after pulverization, wherein the ultrafine simvastatin powder and pregelatinized starch were first mixed according to a continuous mixing method and then pulverized, the raw material supply speed was 8 kg/min, and the mixing speed was 125 rpm/min;
(3)然后,将所得粉碎混合物与微晶纤维素、乳糖、交联羧甲基纤维素钠混合后,再喷入部分预胶化淀粉,然后在干法制粒机内进行制粒,干法制粒机的压辊压力为8~10MPa,压辊间隙0.6~0.9mm,压辊转速15~20r/min,三元旋振筛转速为100~120r/min,制粒过程中添加硬脂酸镁提高颗粒的流动性和成形性,制粒完成后,将颗粒输送到干燥设备中进行干燥,干燥温度为45~55℃,所得颗粒的干燥失重≤5.0%,喷雾干燥结束,将所制颗粒过筛整粒,获得的颗粒粒径为60目;(3) Then, the obtained pulverized mixture is mixed with microcrystalline cellulose, lactose, and cross-linked sodium carboxymethyl cellulose, and then a portion of pregelatinized starch is sprayed into the mixture, and then granulated in a dry granulator. The roller pressure of the dry granulator is 8-10 MPa, the roller gap is 0.6-0.9 mm, the roller speed is 15-20 r/min, and the three-element rotary vibrating screen speed is 100-120 r/min. Magnesium stearate is added during the granulation process to improve the fluidity and formability of the granules. After the granulation is completed, the granules are transported to a drying device for drying at a drying temperature of 45-55° C. The drying loss of the obtained granules is ≤5.0%. After the spray drying is completed, the obtained granules are sieved to obtain granules with a particle size of 60 mesh;
(4)然后,加入羧甲淀粉钠、硬脂酸镁、麦芽糖、硅酸钙,混合均匀,将所制颗粒压制成片芯;(4) Then, sodium carboxymethyl starch, magnesium stearate, maltose, and calcium silicate are added, mixed evenly, and the prepared granules are pressed into tablet cores;
(5)最后,将所得片芯进行薄膜包衣,得到辛伐他汀片剂,所得辛伐他汀片剂每片的重量约为0.12g。(5) Finally, the obtained tablet cores are film-coated to obtain simvastatin tablets, and the weight of each simvastatin tablet obtained is about 0.12 g.
按如下份数准备原料:辛伐他汀35重量份、部分预胶化淀粉15重量份、填充剂75重量份(微晶纤维素35重量份、乳糖18重量份、交联羧甲基纤维素钠22重量份)、硬脂酸镁9重量份、药用辅料18重量份 (羧甲淀粉钠9重量份、硬脂酸镁3重量份、麦芽糖3重量份、硅酸钙3重量份)。Prepare raw materials according to the following amounts: 35 parts by weight of simvastatin, 15 parts by weight of partially pregelatinized starch, 75 parts by weight of filler (35 parts by weight of microcrystalline cellulose, 18 parts by weight of lactose, 22 parts by weight of cross-linked sodium carboxymethyl cellulose), 9 parts by weight of magnesium stearate, and 18 parts by weight of pharmaceutical excipients (9 parts by weight of sodium starch glycolate, 3 parts by weight of magnesium stearate, 3 parts by weight of maltose, and 3 parts by weight of calcium silicate).
(1)将辛伐他汀采用超声波粉碎机进行振动粉碎,得到比表面积为2050m2/kg的辛伐他汀超微粉;(1) pulverizing simvastatin by vibration using an ultrasonic pulverizer to obtain simvastatin ultrafine powder with a specific surface area of 2050 m2/kg;
(2)将微粉后辛伐他汀与预胶化淀粉采用涡轮自冷式无尘粉碎机进行粉碎,粉碎后过144目筛,其中,辛伐他汀超微粉与预胶化淀粉先按照连续混合法进行混合后再进行粉碎,原料供给速度为8kg/min,混合速度为125rpm/min;(2) The micronized simvastatin and pregelatinized starch were pulverized by a turbine self-cooling dust-free pulverizer and passed through a 144-mesh sieve after pulverization, wherein the ultrafine simvastatin powder and pregelatinized starch were first mixed according to a continuous mixing method and then pulverized, the raw material supply speed was 8 kg/min, and the mixing speed was 125 rpm/min;
(3)然后,将所得粉碎混合物与微晶纤维素、乳糖、交联羧甲基纤维素钠混合后,再喷入部分预胶化淀粉,然后在干法制粒机内进行制粒,干法制粒机的压辊压力为8~10MPa,压辊间隙0.6~0.9mm,压辊转速15~20r/min,三元旋振筛转速为100~120r/min,制粒过程中添加硬脂酸镁提高颗粒的流动性和成形性,制粒完成后,将颗粒输送到干燥设备中进行干燥,干燥温度为45~55℃,所得颗粒的干燥失重≤5.0%,喷雾干燥结束,将所制颗粒过筛整粒,获得的颗粒粒径为60目;(3) Then, the obtained pulverized mixture is mixed with microcrystalline cellulose, lactose, and cross-linked sodium carboxymethyl cellulose, and then a portion of pregelatinized starch is sprayed into the mixture, and then granulated in a dry granulator. The roller pressure of the dry granulator is 8-10 MPa, the roller gap is 0.6-0.9 mm, the roller speed is 15-20 r/min, and the three-element rotary vibrating screen speed is 100-120 r/min. Magnesium stearate is added during the granulation process to improve the fluidity and formability of the granules. After the granulation is completed, the granules are transported to a drying device for drying at a drying temperature of 45-55° C. The drying loss of the obtained granules is ≤5.0%. After the spray drying is completed, the obtained granules are sieved to obtain granules with a particle size of 60 mesh;
(4)然后,加入羧甲淀粉钠、硬脂酸镁、麦芽糖、硅酸钙,混合均匀,将所制颗粒压制成片芯;(4) Then, sodium carboxymethyl starch, magnesium stearate, maltose, and calcium silicate are added, mixed evenly, and the prepared granules are pressed into tablet cores;
(5)最后,将所得片芯进行薄膜包衣,得到辛伐他汀片剂,所得辛伐他汀片剂每片的重量约为0.12g。(5) Finally, the obtained tablet cores are film-coated to obtain simvastatin tablets, and the weight of each simvastatin tablet obtained is about 0.12 g.
按如下份数准备原料:辛伐他汀10重量份、部分预胶化淀粉10重量份、填充剂20重量份(微晶纤维素10重量份、乳糖4重量份、交联羧甲基纤维素钠6重量份)、硬脂酸镁3重量份、药用辅料10重量份 (羧甲淀粉钠4重量份、硬脂酸镁2重量份、麦芽糖1重量份、硅酸钙3重量份)。Prepare the raw materials according to the following amounts: 10 parts by weight of simvastatin, 10 parts by weight of partially pregelatinized starch, 20 parts by weight of filler (10 parts by weight of microcrystalline cellulose, 4 parts by weight of lactose, 6 parts by weight of cross-linked sodium carboxymethyl cellulose), 3 parts by weight of magnesium stearate, and 10 parts by weight of pharmaceutical excipients (4 parts by weight of sodium carboxymethyl starch, 2 parts by weight of magnesium stearate, 1 part by weight of maltose, and 3 parts by weight of calcium silicate).
(1)将辛伐他汀采用超声波粉碎机进行振动粉碎,得到比表面积为2050m2/kg的辛伐他汀超微粉;(1) pulverizing simvastatin by vibration using an ultrasonic pulverizer to obtain simvastatin ultrafine powder with a specific surface area of 2050 m2/kg;
(2)将微粉后辛伐他汀与预胶化淀粉采用涡轮自冷式无尘粉碎机进行粉碎,粉碎后过144目筛,其中,辛伐他汀超微粉与预胶化淀粉先按照连续混合法进行混合后再进行粉碎,原料供给速度为8kg/min,混合速度为125rpm/min;(2) The micronized simvastatin and pregelatinized starch were pulverized by a turbine self-cooling dust-free pulverizer and passed through a 144-mesh sieve after pulverization, wherein the ultrafine simvastatin powder and pregelatinized starch were first mixed according to a continuous mixing method and then pulverized, the raw material supply speed was 8 kg/min, and the mixing speed was 125 rpm/min;
(3)然后,将所得粉碎混合物与微晶纤维素、乳糖、交联羧甲基纤维素钠混合后,再喷入部分预胶化淀粉,然后在干法制粒机内进行制粒,干法制粒机的压辊压力为8~10MPa,压辊间隙0.6~0.9mm,压辊转速15~20r/min,三元旋振筛转速为100~120r/min,制粒过程中添加硬脂酸镁提高颗粒的流动性和成形性,制粒完成后,将颗粒输送到干燥设备中进行干燥,干燥温度为45~55℃,所得颗粒的干燥失重≤5.0%,喷雾干燥结束,将所制颗粒过筛整粒,获得的颗粒粒径为60目;(3) Then, the obtained pulverized mixture is mixed with microcrystalline cellulose, lactose, and cross-linked sodium carboxymethyl cellulose, and then a portion of pregelatinized starch is sprayed into the mixture, and then granulated in a dry granulator. The roller pressure of the dry granulator is 8-10 MPa, the roller gap is 0.6-0.9 mm, the roller speed is 15-20 r/min, and the three-element rotary vibrating screen speed is 100-120 r/min. Magnesium stearate is added during the granulation process to improve the fluidity and formability of the granules. After the granulation is completed, the granules are transported to a drying device for drying at a drying temperature of 45-55° C. The drying loss of the obtained granules is ≤5.0%. After the spray drying is completed, the obtained granules are sieved to obtain granules with a particle size of 60 mesh;
(4)然后,加入羧甲淀粉钠、硬脂酸镁、麦芽糖、硅酸钙,混合均匀,将所制颗粒压制成片芯;(4) Then, sodium carboxymethyl starch, magnesium stearate, maltose, and calcium silicate are added, mixed evenly, and the prepared granules are pressed into tablet cores;
(5)最后,将所得片芯进行薄膜包衣,得到辛伐他汀片剂,所得辛伐他汀片剂每片的重量约为0.12g。(5) Finally, the obtained tablet cores are film-coated to obtain simvastatin tablets, and the weight of each simvastatin tablet obtained is about 0.12 g.
将本发明实施例1、2、3所制备的辛伐他汀片剂与市面销售的辛伐他汀片有关物质进行对比试验,结果如图2表格所示The simvastatin tablets prepared in Examples 1, 2, and 3 of the present invention were compared with the related substances of simvastatin tablets sold on the market. The results are shown in the table in FIG.
本发明的实施方式并不限于上述实施例所述,在不偏离本发明的精神和范围的情况下,本领域普通技术人员可以在形式和细节上对本发明做出各种改变和改进,而这些均被认为落入了本发明的保护范围。The implementation of the present invention is not limited to the above embodiments. Without departing from the spirit and scope of the present invention, ordinary technicians in this field can make various changes and improvements to the present invention in form and detail, and these are considered to fall within the protection scope of the present invention.
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