WO2022222205A1 - Amoxicillin capsule and preparation method therefor - Google Patents

Amoxicillin capsule and preparation method therefor Download PDF

Info

Publication number
WO2022222205A1
WO2022222205A1 PCT/CN2021/093201 CN2021093201W WO2022222205A1 WO 2022222205 A1 WO2022222205 A1 WO 2022222205A1 CN 2021093201 W CN2021093201 W CN 2021093201W WO 2022222205 A1 WO2022222205 A1 WO 2022222205A1
Authority
WO
WIPO (PCT)
Prior art keywords
amoxicillin
powder
particle size
heavy
mixing
Prior art date
Application number
PCT/CN2021/093201
Other languages
French (fr)
Chinese (zh)
Inventor
陈海刚
王玉娟
陈晞
刘超
罗秀莲
高嘉璐
Original Assignee
海南通用三洋药业有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 海南通用三洋药业有限公司 filed Critical 海南通用三洋药业有限公司
Publication of WO2022222205A1 publication Critical patent/WO2022222205A1/en

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/4841Filling excipients; Inactive ingredients
    • A61K9/4858Organic compounds
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/41Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having five-membered rings with two or more ring hetero atoms, at least one of which being nitrogen, e.g. tetrazole
    • A61K31/425Thiazoles
    • A61K31/429Thiazoles condensed with heterocyclic ring systems
    • A61K31/43Compounds containing 4-thia-1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula, e.g. penicillins, penems
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/4808Preparations in capsules, e.g. of gelatin, of chocolate characterised by the form of the capsule or the structure of the filling; Capsules containing small tablets; Capsules with outer layer for immediate drug release
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/4883Capsule finishing, e.g. dyeing, aromatising, polishing
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P1/00Drugs for disorders of the alimentary tract or the digestive system
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P11/00Drugs for disorders of the respiratory system
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P11/00Drugs for disorders of the respiratory system
    • A61P11/02Nasal agents, e.g. decongestants
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P11/00Drugs for disorders of the respiratory system
    • A61P11/04Drugs for disorders of the respiratory system for throat disorders
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P13/00Drugs for disorders of the urinary system
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P27/00Drugs for disorders of the senses
    • A61P27/16Otologicals
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A61P31/04Antibacterial agents
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/30Against vector-borne diseases, e.g. mosquito-borne, fly-borne, tick-borne or waterborne diseases whose impact is exacerbated by climate change

Definitions

  • the invention relates to the preparation of capsules, in particular to an amoxicillin capsule and a preparation method thereof.
  • Amoxicillin also known as amoxicillin or amoxicillin, is one of the most commonly used semi-synthetic penicillin broad-spectrum beta-lactam antibiotics, clinically used for the treatment of tonsillitis, laryngitis, pneumonia, chronic bronchitis, urinary Systemic infections, skin and soft tissue infections, purulent pleurisy, hepatobiliary system infections, sepsis, typhoid fever, dysentery, etc.
  • the oral dosage forms of amoxicillin mainly include tablets, capsules, granules, etc., and amoxicillin capsules are mainly used clinically as therapeutic drugs.
  • amoxicillin Due to the poor solubility of amoxicillin, it is slightly soluble in water and insoluble in ethanol, resulting in the problem of poor dissolution of the amoxicillin capsules made. The poor dissolution rate further limits the in vivo absorption of amoxicillin. Therefore, improving the dissolution rate of amoxicillin capsules has always been a research hotspot.
  • amoxicillin itself is sensitive to humidity and heat. High temperature and high humidity will lead to the production of polymers and impurities. The reduction of the content of polymers and impurities is also one of the important factors to be investigated in the preparation of amoxicillin capsules.
  • the Chinese invention patent with the announcement number CN107875136 B discloses a pharmaceutical preparation of amoxicillin and a preparation method thereof.
  • Amoxicillin capsules are prepared by mixing amoxicillin and magnesium stearate, which reduces the types of excipients, thereby reducing the cost of amoxicillin. Security risks.
  • the technical solution uses amoxicillin heavy powder to prepare capsules, but due to the relatively large relative particle size of the amoxicillin heavy powder, there is a phenomenon of uneven mixing, and the technical solution lacks disintegrants, etc. Excipients, resulting in poor dissolution of the prepared amoxicillin capsules.
  • a Chinese invention patent application with publication number CN109172539 A discloses a kind of amoxicillin capsule and its production method and application.
  • the technical scheme adjusts the ratio of amoxicillin heavy powder and light powder , the amount of light powder is increased, but the amount of light powder and the minimum particle size are clearly limited. This is because in the mixing process, there is the phenomenon of light powder floating up and heavy powder sinking, and heavy powder and light powder are very different.
  • the Chinese invention patent application with publication number CN109953971 A discloses a preparation method of amoxicillin capsules, which selects 20-60 mesh amoxicillin heavy powder and more than 60 mesh amoxicillin light powder to mix, although the surface increases
  • the dosage of amoxicillin light powder above 60 mesh is not limited and the minimum particle size is not limited, but it defines amoxicillin powder above 60 mesh as light powder, and uses 20 and 60 mesh sieves as rotary vibrating sieves in the granulation process.
  • the number of sieve meshes, the amount of light powder above 80 meshes contained in the amoxicillin light powder prepared in this way will be substantially reduced, and the technical solution reduces the difficulty of mixing heavy powder and light powder in this way, thereby improving The stability of amoxicillin capsules, but its dissolution rate needs to be improved.
  • the present invention provides an amoxicillin capsule and a preparation method thereof.
  • An amoxicillin capsule the raw materials for making its active ingredients, include: 100 parts by weight of amoxicillin medicinal powder and 0.2-0.5 parts by weight of magnesium stearate;
  • the amoxicillin medicinal powder is composed of 10-35wt% amoxicillin light powder with a particle size of less than 0.180mm (passing an 80-mesh sieve), and 10-40wt% with a particle size of 0.600-0.850mm (passing a 20-mesh sieve and failing to pass a 30-mesh sieve). ) of the amoxicillin heavy powder and the balance of the amoxicillin heavy powder with a particle size of 0.180 to 0.600 mm (passing a 30-mesh sieve and not passing an 80-mesh sieve).
  • amoxicillin powder is obtained by using a dry granulator with a roller pressure of 6.0-10.0 MPa.
  • the ambient humidity is 52-58%.
  • the technological parameters of the dry granulator are: the stirring speed is 15-20 rpm, the screw feeding speed is 50-60 rpm, the pressing roller speed is 10-15 rpm, the pressing roller temperature is 20-30 °C, and the granulation speed is 100 ⁇ 130rpm, the mesh size of the whole grain screen is 0.80 ⁇ 0.84mm, and the mesh number of the rotary vibrating screen is 20 mesh, 30 mesh and 80 mesh.
  • magnesium stearate is 0.180-0.850 mm (passed through 20 mesh sieve, but failed to pass through 80 mesh sieve).
  • a preparation method of amoxicillin capsules is to take amoxicillin medicinal powder and mix with heavy powder, then alternately feed and mix with magnesium stearate, and then fill and polish to obtain the amoxicillin capsules.
  • the humidity of the heavy powder mixing and the mixing material are both 52-58%.
  • the rotating speed of the heavy powder mixing is 12-15 r/min, and the time is 11-15 min; the rotating speed of the mixing is 12-15 r/min, and the time is 2-5 min.
  • the obtained amoxicillin powder needs to stand for 5-10 minutes, and then is taken out and alternately fed with magnesium stearate.
  • the humidity of the filling and polishing are both 30-43%.
  • the dosage of the amoxicillin light powder is increased, and the minimum particle size of the light powder is no longer limited, but the maximum particle size of the heavy powder is limited, thereby obtaining a kind of high stability and dissolution Good Amoxicillin Capsules;
  • the present invention reduces the adverse reactions caused by pharmaceutical excipients by reducing the dosage of magnesium stearate
  • the present invention reduces the granulation pressure by adjusting the process parameters of dry granulation, thereby reducing the decomposition of amoxicillin; by controlling the humidity in the granulation process, while ensuring the stability of the amoxicillin powder (non-polymerization, non-hydrolysis, No impurities), reduce the flying of amoxicillin light powder;
  • the amoxicillin medicinal powder is mixed with the heavy powder first, and the process parameters such as humidity and rotational speed in the heavy powder mixing process are controlled, so as to ensure the stability of the amoxicillin medicinal powder, and effectively suppress the heavy powder from sinking and the light powder on the light powder.
  • the floating phenomenon achieves the purpose of fully mixing heavy powder and light powder;
  • the present invention shortens the mixing time of the magnesium stearate and the amoxicillin powder and improves the drug dissolution rate by first mixing the amoxicillin medicinal powder uniformly, and then mixing with the magnesium stearate in batches alternately.
  • the improvement of the dissolution rate here may be due to the reason that the excessive mixing of magnesium stearate and the powder will affect the dissolution rate of the drug;
  • 1 to 4 are the dissolution curves of the amoxicillin capsules prepared in Examples 1 to 6 and Comparative Examples 1 to 13 in Experimental Example 1 of the present invention in a pH 4.0 acetate buffer;
  • Figures 5 to 8 are the dissolution curves of the amoxicillin capsules prepared in Examples 1 to 6 and Comparative Examples 1 to 13 in Experimental Example 1 of the present invention in a pH 6.8 phosphate buffer;
  • Embodiment 1 A kind of preparation method of amoxicillin capsule
  • the present embodiment is a preparation method of amoxicillin capsules, and the specific preparation process includes the following steps performed in sequence:
  • the stirring speed is 17 rpm
  • the screw feeding speed is 56 rpm
  • the pressure of the pressing roller is 6.8 MPa
  • the rotational speed of the pressing roller is 13 rpm
  • the temperature of the pressing roller is 25 °C
  • the granulating speed is 130 rpm
  • the granulating speed is 130 rpm.
  • the aperture of the particle screen is 0.84mm
  • the mesh number of the rotary vibrating screen is 20 mesh, 30 mesh and 80 mesh.
  • the amoxicillin crude drug was dried in nitrogen at 25°C for 30s, then added to the hopper of a dry granulator for granulation, and collected through a 20-mesh sieve and failed to pass.
  • Amoxicillin heavy powder (particle size is 0.600 ⁇ 0.850mm) with 30 mesh sieve, amoxicillin heavy powder (particle size is 0.180 ⁇ 0.600mm) passed through 30 mesh sieve and not passed through 80 mesh sieve, and amoxicillin heavy powder (particle size is 0.180 ⁇ 0.600mm) passed through 80 mesh sieve
  • amoxicillin light powder (particle size less than 0.180mm)
  • the amoxicillin API that did not pass the 20-mesh sieve was added to the dry granulator for simultaneous granulation.
  • alternate feeding refers to first put in 50g amoxicillin powder, then put in 0.1g magnesium stearate, then put in 50g amoxicillin powder, then put in 0.1g magnesium stearate, and then alternately feed the above-mentioned dosage until the feeding is completed, also That is to say, the amoxicillin powder and the magnesium stearate are cross-feeding, and each material is divided into five feedings. Although the present embodiment is divided into five feedings, it is not limited to being divided into five feedings.
  • amoxicillin capsules also need to be aluminum-plasticized and packaged.
  • Embodiment 2 ⁇ 6 The preparation method of amoxicillin capsule
  • Embodiments 2 to 6 are respectively a preparation method of amoxicillin capsules, and their steps are basically the same as those of embodiment 1, and the difference is only in the amount of raw materials and process parameters. For details, see Table 1:
  • amoxicillin capsules prepared in Examples 1-6 have good stability and high dissolution rate.
  • Comparative Examples 1 to 10 are comparative tests of the preparation process of amoxicillin capsules in Example 1, and the differences are only:
  • Comparative example 8 no longer distinguishes heavy powder mixing and compounding and carries out two-step mixing, but mixes magnesium stearate with the amoxicillin powder of each particle size together;
  • mixing time is 8min
  • Example 1 38.61 54.27 65.35 75.14 86.19 97.1 100.09 100.1
  • Example 2 39.27 56.72 68.14 78.25 88.14 99.62 100.02 100.02
  • Example 3 37.41 52.12 63.59 74.15 85.11 96.75 99.98 99.98 Example 4 38.21 53.79 64.85 74.67 85.45 96.96 100.07 100.03
  • Example 5 38.19 55.11 65.98 75.37 86.57 98.28 100.01 100.02
  • Example 6 39.02 55.41 67.66 76.45 85.79 98.79 100.04 100.03
  • Comparative Example 1 38.99 56.42 68.76 77.91 87.64 96.75 98.77 98.77 Comparative Example 2 12.1 27.54 40.67 50.12 59.89 64.18 70.21 80.16
  • Comparative Example 3 36.44 51.85 63.27 74.39 85.21 96.43 99.88 99.87 Comparative Example 4 32.45 50.97 60.27 72.44 81.69 92.74 99.63 99.6 Comparative Example 5 25.31 38.64
  • amoxicillin capsules (specification 0.5g) prepared in Examples 1 to 6 and Comparative Examples 1 to 13, and place them for 6 months under the conditions of 40 ⁇ 2° C. and RH75 ⁇ 5% respectively. Sampling at 2, 3 and 6 months, tested according to the stability check items, and compared with the 0-day data.
  • Amoxicillin Capsules were tested in accordance with the indicators and determination methods of sample content, moisture, related substances, dissolution rate, etc. stipulated in the 2015 edition of the Chinese Pharmacopoeia. The specific test results are shown in the following table:
  • the amoxicillin capsules prepared in Comparative Examples 1-13 cannot have both good dissolution and stability at the same time, and the content of related substances is relatively high, while the amoxicillin capsules prepared in Examples 1-6 of the present invention Xilin capsules have good stability and dissolution, and the content of related substances is low.
  • the above experiments show that the present invention produces less impurities in the process of preparing amoxicillin capsules, which is more conducive to the preparation and storage of amoxicillin capsules.
  • amoxicillin capsules prepared by the present invention can have both good dissolution and stability, and the content of related substances is low.

Landscapes

  • Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Veterinary Medicine (AREA)
  • Medicinal Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
  • Epidemiology (AREA)
  • Pulmonology (AREA)
  • Otolaryngology (AREA)
  • Communicable Diseases (AREA)
  • Oncology (AREA)
  • Urology & Nephrology (AREA)
  • Medicinal Preparation (AREA)

Abstract

Provided in the present invention are an amoxicillin capsule and a preparation method therefor, belonging to the technical field of drug preparation. 10-35 wt% of light amoxicillin powder with a particle size of less than 0.180 mm and 10-40 wt% of heavy amoxicillin powder with a particle size of 0.600-0.850 mm are mixed with the balance of heavy amoxicillin powder with a particle size of 0.180-0.600 mm, then the mixture and magnesium stearate are fed alternately for mixing, and filling and polishing are performed to obtain an amoxicillin capsule. According to the present invention, the particle size ratio of the amoxicillin powder is adjusted, the amount of the light amoxicillin powder is increased, and the minimum particle size of the light powder is no longer limited whereas the maximum particle size of the heavy powder is limited, so that an amoxicillin capsule with a high stability and good dissolution rate is obtained.

Description

阿莫西林胶囊及其制备方法Amoxicillin capsules and preparation method thereof 技术领域technical field
本发明涉及胶囊的制备,尤其涉及一种阿莫西林胶囊及其制备方法。The invention relates to the preparation of capsules, in particular to an amoxicillin capsule and a preparation method thereof.
背景技术Background technique
阿莫西林,又名安莫西林或安默西林,是一种最常用的半合成青霉素类广谱β-内酰胺类抗生素,临床用于治疗扁桃体炎、喉炎、肺炎、慢性支气管炎、泌尿系统感染、皮肤软组织感染、化脓性胸膜炎、肝胆系统感染、败血症、伤寒、痢疾等。目前,阿莫西林口服剂型主要包括片剂、胶囊剂、颗粒剂等,临床上主要使用阿莫西林胶囊作为治疗药物。Amoxicillin, also known as amoxicillin or amoxicillin, is one of the most commonly used semi-synthetic penicillin broad-spectrum beta-lactam antibiotics, clinically used for the treatment of tonsillitis, laryngitis, pneumonia, chronic bronchitis, urinary Systemic infections, skin and soft tissue infections, purulent pleurisy, hepatobiliary system infections, sepsis, typhoid fever, dysentery, etc. At present, the oral dosage forms of amoxicillin mainly include tablets, capsules, granules, etc., and amoxicillin capsules are mainly used clinically as therapeutic drugs.
由于阿莫西林溶解性较差,在水中微溶、乙醇中难溶,导致制成的阿莫西林胶囊存在溶出度差的问题。溶出度差又进一步限制了阿莫西林的体内吸收,因此,提高阿莫西林胶囊溶出度一直是研究的热点。此外,阿莫西林自身对湿、热较敏感,高温高湿都会导致其产生聚合物和杂质,对于聚合物和杂质含量的降低也是制备阿莫西林胶囊需要考察的重要因素之一。Due to the poor solubility of amoxicillin, it is slightly soluble in water and insoluble in ethanol, resulting in the problem of poor dissolution of the amoxicillin capsules made. The poor dissolution rate further limits the in vivo absorption of amoxicillin. Therefore, improving the dissolution rate of amoxicillin capsules has always been a research hotspot. In addition, amoxicillin itself is sensitive to humidity and heat. High temperature and high humidity will lead to the production of polymers and impurities. The reduction of the content of polymers and impurities is also one of the important factors to be investigated in the preparation of amoxicillin capsules.
公告号为CN107875136 B的中国发明专利中公开了一种阿莫西林药物制剂及其制备方法,其采用阿莫西林和硬脂酸镁混合制备阿莫西林胶囊,减少了辅料的种类,从而降低了安全隐患。但为保证药物稳定性,该技术方案选用阿莫西林重粉制备胶囊,但由于阿莫西林重粉的相对粒度较大,存在混合不均匀的现象,且该技术方案中又缺乏崩解剂等辅料,导致制备的阿莫西林胶囊溶出度较差。The Chinese invention patent with the announcement number CN107875136 B discloses a pharmaceutical preparation of amoxicillin and a preparation method thereof. Amoxicillin capsules are prepared by mixing amoxicillin and magnesium stearate, which reduces the types of excipients, thereby reducing the cost of amoxicillin. Security risks. However, in order to ensure the stability of the drug, the technical solution uses amoxicillin heavy powder to prepare capsules, but due to the relatively large relative particle size of the amoxicillin heavy powder, there is a phenomenon of uneven mixing, and the technical solution lacks disintegrants, etc. Excipients, resulting in poor dissolution of the prepared amoxicillin capsules.
公布号为CN109172539 A的中国发明专利申请中公开了一种阿莫西林胶囊及其生产方法和应用,为提高阿莫西林的溶出度,该技术方案调整了阿 莫西林重粉与轻粉的比例,增大了轻粉用量,但对轻粉用量及最小粒径进行了明确限制,这是由于在混料过程中,存在轻粉上飘、重粉下沉的现象,重粉和轻粉很难混匀,而轻粉用量的增加,则会导致轻粉与重粉更难混匀,轻粉聚集,而轻粉聚集部分的比表面积较大,比表面积的增加则会导致其与水分接触机率增大,从而使杂质增多,制出的阿莫西林胶囊稳定性较差。A Chinese invention patent application with publication number CN109172539 A discloses a kind of amoxicillin capsule and its production method and application. In order to improve the dissolution rate of amoxicillin, the technical scheme adjusts the ratio of amoxicillin heavy powder and light powder , the amount of light powder is increased, but the amount of light powder and the minimum particle size are clearly limited. This is because in the mixing process, there is the phenomenon of light powder floating up and heavy powder sinking, and heavy powder and light powder are very different. It is difficult to mix, and the increase of the amount of light powder will make it more difficult to mix the light powder and the heavy powder, and the light powder will aggregate, and the specific surface area of the light powder aggregated part will be larger, and the increase of the specific surface area will cause it to come into contact with water. The probability increases, so that the impurities increase, and the stability of the prepared amoxicillin capsules is poor.
公布号为CN109953971 A的中国发明专利申请中公开了一种阿莫西林胶囊的制备方法,其选用20~60目的阿莫西林重粉与60目以上的阿莫西林轻粉混合,虽然表面上增加了60目以上阿莫西林轻粉用量且未限制最小粒径,但其将60目以上的阿莫西林药粉都定义为轻粉,并在制粒过程中以20和60目筛为旋振筛筛网目数,这样制备的阿莫西林轻粉中含有的80目以上轻粉的量实质上则会明显降低,该技术方案通过这种方式,降低了重粉与轻粉混合难度,从而提高阿莫西林胶囊的稳定性,但其溶出度还有待提高。The Chinese invention patent application with publication number CN109953971 A discloses a preparation method of amoxicillin capsules, which selects 20-60 mesh amoxicillin heavy powder and more than 60 mesh amoxicillin light powder to mix, although the surface increases The dosage of amoxicillin light powder above 60 mesh is not limited and the minimum particle size is not limited, but it defines amoxicillin powder above 60 mesh as light powder, and uses 20 and 60 mesh sieves as rotary vibrating sieves in the granulation process. The number of sieve meshes, the amount of light powder above 80 meshes contained in the amoxicillin light powder prepared in this way will be substantially reduced, and the technical solution reduces the difficulty of mixing heavy powder and light powder in this way, thereby improving The stability of amoxicillin capsules, but its dissolution rate needs to be improved.
发明内容SUMMARY OF THE INVENTION
针对上述问题,本发明提供一种阿莫西林胶囊及其制备方法。In view of the above problems, the present invention provides an amoxicillin capsule and a preparation method thereof.
为实现上述目的,本发明所采用的技术方案为:For achieving the above object, the technical scheme adopted in the present invention is:
一种阿莫西林胶囊,制成它的有效成分的原料,包括:100重量份的阿莫西林药粉和0.2~0.5重量份硬脂酸镁;An amoxicillin capsule, the raw materials for making its active ingredients, include: 100 parts by weight of amoxicillin medicinal powder and 0.2-0.5 parts by weight of magnesium stearate;
所述阿莫西林药粉是由10~35wt%粒度小于0.180mm(通过80目筛)的阿莫西林轻粉、10~40wt%粒度为0.600~0.850mm(通过20目筛且未通过30目筛)的阿莫西林重粉和余量的粒度为0.180~0.600mm(通过30目筛且未通过80目筛)的阿莫西林重粉组成。The amoxicillin medicinal powder is composed of 10-35wt% amoxicillin light powder with a particle size of less than 0.180mm (passing an 80-mesh sieve), and 10-40wt% with a particle size of 0.600-0.850mm (passing a 20-mesh sieve and failing to pass a 30-mesh sieve). ) of the amoxicillin heavy powder and the balance of the amoxicillin heavy powder with a particle size of 0.180 to 0.600 mm (passing a 30-mesh sieve and not passing an 80-mesh sieve).
进一步的,所述阿莫西林药粉是使用压辊压力为6.0~10.0MPa的干法制 粒机制得。Further, the amoxicillin powder is obtained by using a dry granulator with a roller pressure of 6.0-10.0 MPa.
进一步的,在所述干法制粒机制粒过程中,环境湿度为52~58%。Further, in the granulation process of the dry granulator, the ambient humidity is 52-58%.
进一步的,所述干法制粒机的工艺参数为:搅拌转速为15~20rpm,螺旋送料转速为50~60rpm,压辊转速为10~15rpm,压辊温度为20~30℃,整粒转速为100~130rpm,整粒筛网孔径为0.80~0.84mm,旋振筛筛网目数为20目、30目和80目。Further, the technological parameters of the dry granulator are: the stirring speed is 15-20 rpm, the screw feeding speed is 50-60 rpm, the pressing roller speed is 10-15 rpm, the pressing roller temperature is 20-30 ℃, and the granulation speed is 100~130rpm, the mesh size of the whole grain screen is 0.80~0.84mm, and the mesh number of the rotary vibrating screen is 20 mesh, 30 mesh and 80 mesh.
进一步的,硬脂酸镁的粒度为0.180~0.850mm(通过20目筛,但未通过80目筛)。Further, the particle size of magnesium stearate is 0.180-0.850 mm (passed through 20 mesh sieve, but failed to pass through 80 mesh sieve).
一种阿莫西林胶囊的制备方法,是取阿莫西林药粉经重粉混合后,再与硬脂酸镁交替投料进行混料,然后经充填及抛光,即得所述阿莫西林胶囊。A preparation method of amoxicillin capsules is to take amoxicillin medicinal powder and mix with heavy powder, then alternately feed and mix with magnesium stearate, and then fill and polish to obtain the amoxicillin capsules.
进一步的,所述重粉混合和混料的湿度均为52~58%。Further, the humidity of the heavy powder mixing and the mixing material are both 52-58%.
进一步的,所述重粉混合的转速为12~15r/min、时间为11~15min;所述混料的转速为12~15r/min、时间为2~5min。Further, the rotating speed of the heavy powder mixing is 12-15 r/min, and the time is 11-15 min; the rotating speed of the mixing is 12-15 r/min, and the time is 2-5 min.
进一步的,所述重粉混合停止后,所得阿莫西林粉需静置5~10min,再取出与硬脂酸镁进行交替投料。Further, after the mixing of the heavy powder is stopped, the obtained amoxicillin powder needs to stand for 5-10 minutes, and then is taken out and alternately fed with magnesium stearate.
进一步的,所述充填及抛光的湿度均为30~43%。Further, the humidity of the filling and polishing are both 30-43%.
本发明的阿莫西林胶囊的制备方法的有益效果为:The beneficial effects of the preparation method of amoxicillin capsules of the present invention are:
本发明通过调整阿莫西林药粉粒径比例,增加阿莫西林轻粉用量,且不再限制轻粉的最小粒径,但限制了重粉的最大粒径,从而获得一种稳定性高、溶出度好的阿莫西林胶囊;By adjusting the particle size ratio of the amoxicillin medicinal powder, the dosage of the amoxicillin light powder is increased, and the minimum particle size of the light powder is no longer limited, but the maximum particle size of the heavy powder is limited, thereby obtaining a kind of high stability and dissolution Good Amoxicillin Capsules;
本发明通过减少硬脂酸镁的用量,从而降低药物辅料引起的不良反应;The present invention reduces the adverse reactions caused by pharmaceutical excipients by reducing the dosage of magnesium stearate;
本发明通过调整干法制粒的工艺参数,降低制粒压力,从而减少阿莫西 林的分解;通过控制制粒过程中的湿度,在保证阿莫西林药粉稳定性的同时(不聚合、不水解、不产生杂质),减少阿莫西林轻粉飞扬;The present invention reduces the granulation pressure by adjusting the process parameters of dry granulation, thereby reducing the decomposition of amoxicillin; by controlling the humidity in the granulation process, while ensuring the stability of the amoxicillin powder (non-polymerization, non-hydrolysis, No impurities), reduce the flying of amoxicillin light powder;
本发明通过先将阿莫西林药粉进行重粉混合,且控制重粉混合过程中的湿度和转速等工艺参数,在保证阿莫西林药粉稳定性的同时,有效抑制重粉下沉、轻粉上飘现象,达到了重粉与轻粉充分混匀的目的;In the present invention, the amoxicillin medicinal powder is mixed with the heavy powder first, and the process parameters such as humidity and rotational speed in the heavy powder mixing process are controlled, so as to ensure the stability of the amoxicillin medicinal powder, and effectively suppress the heavy powder from sinking and the light powder on the light powder. The floating phenomenon achieves the purpose of fully mixing heavy powder and light powder;
本发明通过先将阿莫西林药粉混匀,再与硬脂酸镁分批交替投料进行混匀的方式,缩短了硬脂酸镁与阿莫西林粉的混料时间,提高了药物溶出度。这里溶出度的提高,可能是由于硬脂酸镁与药粉过度混合会影响药物溶出度的原因;The present invention shortens the mixing time of the magnesium stearate and the amoxicillin powder and improves the drug dissolution rate by first mixing the amoxicillin medicinal powder uniformly, and then mixing with the magnesium stearate in batches alternately. The improvement of the dissolution rate here may be due to the reason that the excessive mixing of magnesium stearate and the powder will affect the dissolution rate of the drug;
通过调整充填及抛光过程中的湿度,增加药物稳定性。Increase drug stability by adjusting the humidity during filling and polishing.
附图说明Description of drawings
图1~4是本发明实验例1中实施例1~6和对比例1~13制备的阿莫西林胶囊在pH4.0醋酸盐缓冲液中的溶出度曲线图;1 to 4 are the dissolution curves of the amoxicillin capsules prepared in Examples 1 to 6 and Comparative Examples 1 to 13 in Experimental Example 1 of the present invention in a pH 4.0 acetate buffer;
图5~8是本发明实验例1中实施例1~6和对比例1~13制备的阿莫西林胶囊在pH6.8磷酸盐缓冲液中的溶出度曲线图;Figures 5 to 8 are the dissolution curves of the amoxicillin capsules prepared in Examples 1 to 6 and Comparative Examples 1 to 13 in Experimental Example 1 of the present invention in a pH 6.8 phosphate buffer;
图9~12是本发明实验例1中实施例1~6和对比例1~13制备的阿莫西林胶囊在水中的溶出度曲线图。9-12 are the dissolution curves of the amoxicillin capsules in water prepared by Examples 1-6 and Comparative Examples 1-13 in Experimental Example 1 of the present invention.
具体实施方式Detailed ways
下面对本发明实施例中的技术方案进行清楚、完整地描述。在下面的描述中阐述了很多具体细节以便于充分理解本发明,但是本发明还可以采用其他不同于在此描述的其它方式来实施,本领域技术人员可以在不违背本发明内涵的情况下做类似推广,因此本发明不受下面公开的具体实施例的限制。The technical solutions in the embodiments of the present invention will be clearly and completely described below. Many specific details are set forth in the following description to facilitate a full understanding of the present invention, but the present invention can also be implemented in other ways different from those described herein, and those skilled in the art can do so without departing from the connotation of the present invention. Similar promotion, therefore, the present invention is not limited by the specific embodiments disclosed below.
实施例1 一种阿莫西林胶囊的制备方法Embodiment 1 A kind of preparation method of amoxicillin capsule
本实施例为一种阿莫西林胶囊的制备方法,具体制备过程包括依次进行的以下步骤:The present embodiment is a preparation method of amoxicillin capsules, and the specific preparation process includes the following steps performed in sequence:
1)设定干法制粒机的设备参数:搅拌转速为17rpm,螺旋送料转速为56rpm,压辊压力为6.8MPa,压辊转速为13rpm,压辊温度为25℃,整粒转速为130rpm,整粒筛网孔径为0.84mm,旋振筛筛网目数为20目、30目和80目1) Set the equipment parameters of the dry granulator: the stirring speed is 17 rpm, the screw feeding speed is 56 rpm, the pressure of the pressing roller is 6.8 MPa, the rotational speed of the pressing roller is 13 rpm, the temperature of the pressing roller is 25 ℃, the granulating speed is 130 rpm, and the granulating speed is 130 rpm. The aperture of the particle screen is 0.84mm, and the mesh number of the rotary vibrating screen is 20 mesh, 30 mesh and 80 mesh.
于温度为25℃、湿度为52%的条件下,取阿莫西林原料药经25℃的氮气干燥30s后,加至干法制粒机料斗中进行制粒,分别收集通过20目筛且未通过30目筛的阿莫西林重粉(粒度为0.600~0.850mm)、通过30目筛且未通过80目筛的阿莫西林重粉(粒度为0.180~0.600mm)和通过80目筛的阿莫西林轻粉(粒度小于0.180mm),对于未通过20目筛的阿莫西林原料药重新加入干法制粒机进行同步制粒。Under the conditions of a temperature of 25°C and a humidity of 52%, the amoxicillin crude drug was dried in nitrogen at 25°C for 30s, then added to the hopper of a dry granulator for granulation, and collected through a 20-mesh sieve and failed to pass. Amoxicillin heavy powder (particle size is 0.600~0.850mm) with 30 mesh sieve, amoxicillin heavy powder (particle size is 0.180~0.600mm) passed through 30 mesh sieve and not passed through 80 mesh sieve, and amoxicillin heavy powder (particle size is 0.180~0.600mm) passed through 80 mesh sieve For the amoxicillin light powder (particle size less than 0.180mm), the amoxicillin API that did not pass the 20-mesh sieve was added to the dry granulator for simultaneous granulation.
2)于温度为25℃、湿度为52%的条件下,分别称量56.5g粒度小于0.180mm的阿莫西林轻粉(占比22.6wt%)、75g粒度为0.600~0.850mm的阿莫西林重粉(占比30wt%)和118.5g粒度为0.180~0.600mm的阿莫西林重粉(占比47.4wt%),加入到多向运动混合机中,维持25℃、湿度为52%,控制混合转速为14r/min,混合11min,混合机自动停机后,切断电源静置8min,取出阿莫西林粉。2) Under the conditions of a temperature of 25°C and a humidity of 52%, weigh 56.5g of amoxicillin light powder with a particle size of less than 0.180mm (accounting for 22.6wt%) and 75g of amoxicillin with a particle size of 0.600-0.850mm. Heavy powder (accounting for 30wt%) and 118.5g of amoxicillin heavy powder (accounting for 47.4wt%) with a particle size of 0.180-0.600mm were added to a multi-directional motion mixer, maintained at 25°C, humidity of 52%, controlled The mixing speed was 14 r/min, and the mixing was performed for 11 min. After the mixer was automatically shut down, the power was cut off and left to stand for 8 min, and the amoxicillin powder was taken out.
3)于温度为25℃、湿度为52%的条件下,再取250g阿莫西林粉与0.5g硬脂酸镁交替投料进行混料(阿莫西林粉与硬脂酸镁的重量比为100:0.2),维持25℃、湿度为52%,控制混料转速为14r/min,混料2min,得混合药粉;3) under the condition that temperature is 25 ℃, humidity is 52%, get 250g amoxicillin powder and 0.5g magnesium stearate alternately feed and mix (the weight ratio of amoxicillin powder and magnesium stearate is 100 : 0.2), maintain 25 ℃, humidity is 52%, control mixing speed to be 14r/min, mix material 2min, obtain mixed medicine powder;
其中,交替投料是指先投入50g阿莫西林粉,再投入0.1g硬脂酸镁,然后投入50g阿莫西林粉,再投入0.1g硬脂酸镁,依次按上述用量交替投料至投料完毕,也就是说阿莫西林粉与硬脂酸镁交叉投料,每种物料分五次投料,虽然本实施例分五次投料,但并不限于分五次投料。Wherein, alternate feeding refers to first put in 50g amoxicillin powder, then put in 0.1g magnesium stearate, then put in 50g amoxicillin powder, then put in 0.1g magnesium stearate, and then alternately feed the above-mentioned dosage until the feeding is completed, also That is to say, the amoxicillin powder and the magnesium stearate are cross-feeding, and each material is divided into five feedings. Although the present embodiment is divided into five feedings, it is not limited to being divided into five feedings.
4)于温度为25℃、湿度为40%的条件下,取混合药粉用胶囊灌装机灌入明胶空心胶囊中进行充填和抛光,制得1000粒的阿莫西林胶囊;4) under the condition that the temperature is 25°C and the humidity is 40%, get the mixed medicinal powder and pour it into the gelatin hollow capsule with a capsule filling machine for filling and polishing to obtain 1000 amoxicillin capsules;
所得阿莫西林胶囊还需进行铝塑和包装。The obtained amoxicillin capsules also need to be aluminum-plasticized and packaged.
实施例2~6 阿莫西林胶囊的制备方法Embodiment 2~6 The preparation method of amoxicillin capsule
实施例2~6分别为一种阿莫西林胶囊的制备方法,它们的步骤与实施例1基本相同,不同之处仅在于原料用量及工艺参数的不同,具体详见表1:Embodiments 2 to 6 are respectively a preparation method of amoxicillin capsules, and their steps are basically the same as those of embodiment 1, and the difference is only in the amount of raw materials and process parameters. For details, see Table 1:
表1 实施例2~6中各项工艺参数一览表Table 1 List of various process parameters in Examples 2 to 6
Figure PCTCN2021093201-appb-000001
Figure PCTCN2021093201-appb-000001
Figure PCTCN2021093201-appb-000002
Figure PCTCN2021093201-appb-000002
实施例2~6其它部分的内容,与实施例1相同。The contents of other parts of Examples 2 to 6 are the same as those of Example 1.
实施例1~6制备的阿莫西林胶囊稳定性好,溶出度高。The amoxicillin capsules prepared in Examples 1-6 have good stability and high dissolution rate.
实验例1 阿莫西林胶囊的溶出度测定Experimental Example 1 Dissolution Determination of Amoxicillin Capsules
对比例1~10为实施例1中阿莫西林胶囊的制备过程的对比试验,区别仅在于:Comparative Examples 1 to 10 are comparative tests of the preparation process of amoxicillin capsules in Example 1, and the differences are only:
对比例1中使用100g粒度小于0.180mm的阿莫西林轻粉(占比40wt%)、75g粒度为0.600~0.850mm的阿莫西林重粉(占比30wt%)和75g粒度为0.180~0.600mm的阿莫西林重粉制备阿莫西林粉(占比30wt%);In Comparative Example 1, 100 g of amoxicillin light powder with a particle size of less than 0.180 mm (40 wt %), 75 g of amoxicillin heavy powder with a particle size of 0.600 to 0.850 mm (30 wt %) and 75 g of amoxicillin with a particle size of 0.180 to 0.600 mm were used Amoxicillin heavy powder prepared amoxicillin powder (accounting for 30wt%);
对比例2中使用12.5g粒度小于0.180mm的阿莫西林轻粉(占比5wt%)、75g粒度为0.600~0.850mm的阿莫西林重粉(占比30wt%)和162.5g粒度为0.180~0.600mm的阿莫西林重粉制备阿莫西林粉(占比65wt%);In Comparative Example 2, 12.5g of amoxicillin light powder with a particle size of less than 0.180mm (5wt%), 75g of amoxicillin heavy powder with a particle size of 0.600-0.850mm (30wt%) and 162.5g of amoxicillin with a particle size of 0.180- Amoxicillin powder (accounting for 65wt%) is prepared from 0.600mm amoxicillin heavy powder;
对比例3的制粒过程中压辊压力设定为11.0MPa;In the granulation process of Comparative Example 3, the pressure of the pressing roller was set to 11.0 MPa;
对比例4的制粒过程中湿度为63%;The humidity in the granulation process of Comparative Example 4 was 63%;
对比例5的制粒过程中湿度为48%;The humidity in the granulation process of Comparative Example 5 was 48%;
对比例6的重粉混合过程中湿度为63%;The humidity in the heavy powder mixing process of Comparative Example 6 was 63%;
对比例7的重粉混合过程中湿度为48%;The humidity in the heavy powder mixing process of Comparative Example 7 was 48%;
对比例8不再区分重粉混合和混料进行两步混合,而是将硬脂酸镁与各粒度的阿莫西林药粉一起混合;Comparative example 8 no longer distinguishes heavy powder mixing and compounding and carries out two-step mixing, but mixes magnesium stearate with the amoxicillin powder of each particle size together;
对比例9的步骤3)中混料时间为8min;In the step 3 of comparative example 9), mixing time is 8min;
对比例10的充填及抛光过程中湿度为50%;The humidity during filling and polishing of Comparative Example 10 was 50%;
对比例11中按照公告号为CN107875136B的中国发明专利中公开的制备方法制备阿莫西林胶囊;In Comparative Example 11, amoxicillin capsules were prepared according to the preparation method disclosed in the Chinese invention patent with the publication number of CN107875136B;
对比例12中按照公告号为CN109172539A的中国发明专利申请中公开的制备方法制备阿莫西林胶囊;In Comparative Example 12, amoxicillin capsules were prepared according to the preparation method disclosed in the Chinese invention patent application with the publication number of CN109172539A;
对比例13按照公告号为CN109953971A的中国发明专利申请中公开的制备方法制备阿莫西林胶囊。Comparative Example 13 Amoxicillin capsules were prepared according to the preparation method disclosed in the Chinese invention patent application with the publication number of CN109953971A.
需要注意的是,实验发现在制粒过程中,压力低于6.0MPa时无法很好的进行制粒,因此这里不再增设对比例;It should be noted that the experiment found that in the granulation process, when the pressure is lower than 6.0MPa, the granulation cannot be carried out well, so no more comparative examples are added here;
取实施例1~6和对比例1~13制备的阿莫西林胶囊,按照《中国药典》(2015版四部0931)中第一法的规定,分别在pH4.0醋酸盐缓冲液、pH6.8磷酸盐缓冲液及水中进行体外释放度对比试验,试验结果见表2~4和附图1~12:Take the amoxicillin capsules prepared in Examples 1 to 6 and Comparative Examples 1 to 13, according to the provisions of the first method in "Chinese Pharmacopoeia" (2015 edition four parts 0931), respectively in pH4.0 acetate buffer, pH6. 8 The in vitro release comparison test was carried out in phosphate buffer and water, and the test results are shown in Tables 2 to 4 and accompanying drawings 1 to 12:
表2 pH4.0醋酸盐缓冲液中的溶出度数据一览表Table 2 Summary of dissolution data in pH 4.0 acetate buffer
时间(min)time (min) 55 1010 1515 2020 3030 4545 6060 9090
实施例1Example 1 38.6138.61 54.2754.27 65.3565.35 75.1475.14 86.1986.19 97.197.1 100.09100.09 100.1100.1
实施例2Example 2 39.2739.27 56.7256.72 68.1468.14 78.2578.25 88.1488.14 99.6299.62 100.02100.02 100.02100.02
实施例3Example 3 37.4137.41 52.1252.12 63.5963.59 74.1574.15 85.1185.11 96.7596.75 99.9899.98 99.9899.98
实施例4Example 4 38.2138.21 53.7953.79 64.8564.85 74.6774.67 85.4585.45 96.9696.96 100.07100.07 100.03100.03
实施例5Example 5 38.1938.19 55.1155.11 65.9865.98 75.3775.37 86.5786.57 98.2898.28 100.01100.01 100.02100.02
实施例6Example 6 39.0239.02 55.4155.41 67.6667.66 76.4576.45 85.7985.79 98.7998.79 100.04100.04 100.03100.03
对比例1Comparative Example 1 38.9938.99 56.4256.42 68.7668.76 77.9177.91 87.6487.64 96.7596.75 98.7798.77 98.7798.77
对比例2Comparative Example 2 12.112.1 27.5427.54 40.6740.67 50.1250.12 59.8959.89 64.1864.18 70.2170.21 80.1680.16
对比例3Comparative Example 3 36.4436.44 51.8551.85 63.2763.27 74.3974.39 85.2185.21 96.4396.43 99.8899.88 99.8799.87
对比例4Comparative Example 4 32.4532.45 50.9750.97 60.2760.27 72.4472.44 81.6981.69 92.7492.74 99.6399.63 99.699.6
对比例5Comparative Example 5 25.3125.31 38.6438.64 48.6348.63 55.6855.68 66.7266.72 78.0178.01 85.2985.29 96.1196.11
对比例6Comparative Example 6 30.2130.21 47.6447.64 54.9554.95 68.7268.72 79.8179.81 89.0189.01 98.7998.79 98.9898.98
对比例7Comparative Example 7 20.2620.26 34.8334.83 46.5246.52 54.3454.34 66.1266.12 76.3576.35 83.9283.92 94.5994.59
对比例8Comparative Example 8 23.1523.15 42.0542.05 50.8250.82 69.1169.11 80.5980.59 93.1193.11 99.7599.75 99.7499.74
对比例9Comparative Example 9 21.5821.58 43.1543.15 48.9748.97 58.6458.64 72.3372.33 89.6489.64 96.5896.58 99.6799.67
对比例10Comparative Example 10 37.2237.22 52.6352.63 63.2863.28 74.5474.54 85.3685.36 96.9896.98 99.8799.87 99.8799.87
对比例11Comparative Example 11 16.8516.85 31.3331.33 45.2545.25 52.6952.69 62.3562.35 71.1171.11 80.2580.25 90.2690.26
对比例12Comparative Example 12 36.5636.56 51.9851.98 63.8763.87 75.1275.12 86.2586.25 97.997.9 99.6799.67 99.6999.69
对比例13Comparative Example 13 30.2130.21 50.2650.26 60.2560.25 70.8570.85 80.2480.24 90.6390.63 96.8996.89 99.8799.87
表3 pH6.8磷酸盐缓冲液中的溶出度数据一览表Table 3 Summary of dissolution data in pH 6.8 phosphate buffer
时间(min)time (min) 55 1010 1515 2020 3030 4545 6060 9090
实施例1Example 1 53.4353.43 72.6472.64 83.5983.59 93.5693.56 99.999.9 100.06100.06 100.08100.08 100.07100.07
实施例2Example 2 55.1555.15 74.5674.56 85.6185.61 94.2594.25 99.9699.96 100.02100.02 100.01100.01 100.02100.02
实施例3Example 3 54.6354.63 73.0173.01 84.2684.26 93.7593.75 99.9199.91 100100 99.9899.98 99.9899.98
实施例4Example 4 53.6853.68 73.5673.56 83.2683.26 93.9893.98 99.8999.89 100.06100.06 100.07100.07 100.03100.03
实施例5Example 5 53.1653.16 73.5973.59 84.5384.53 94.294.2 99.9299.92 100.01100.01 100.01100.01 100.02100.02
实施例6Example 6 54.1654.16 73.1273.12 84.9884.98 93.4593.45 99.9499.94 100.3100.3 100.04100.04 100.03100.03
对比例1Comparative Example 1 56.2156.21 74.8674.86 85.9985.99 94.5694.56 98.7498.74 98.7398.73 98.7498.74 98.7498.74
对比例2Comparative Example 2 20.0120.01 49.5849.58 66.7466.74 74.2874.28 84.0184.01 95.0495.04 99.6799.67 99.6699.66
对比例3Comparative Example 3 50.5450.54 70.6370.63 81.3681.36 91.5891.58 98.8998.89 99.8799.87 99.8899.88 99.8799.87
对比例4Comparative Example 4 49.5949.59 68.5668.56 77.9977.99 90.1590.15 97.4597.45 99.6299.62 99.6399.63 99.699.6
对比例5Comparative Example 5 39.5439.54 57.9957.99 70.5970.59 86.8986.89 92.9392.93 96.1196.11 98.1498.14 98.1398.13
对比例6Comparative Example 6 48.6948.69 68.1268.12 76.8276.82 91.0191.01 97.2597.25 98.9798.97 98.9998.99 98.9898.98
对比例7Comparative Example 7 35.5635.56 54.3654.36 68.2568.25 88.6688.66 93.5693.56 98.7998.79 98.7998.79 98.898.8
对比例8Comparative Example 8 36.8636.86 56.5456.54 69.6369.63 87.9187.91 93.4593.45 99.7399.73 99.7599.75 99.7499.74
对比例9Comparative Example 9 34.7734.77 52.0152.01 64.6964.69 85.3685.36 90.1190.11 99.6799.67 99.6799.67 99.6799.67
对比例10Comparative Example 10 51.2551.25 72.5972.59 83.0183.01 92.9992.99 99.8799.87 99.8799.87 99.8699.86 99.8799.87
对比例11Comparative Example 11 22.5622.56 50.2150.21 65.9765.97 75.6575.65 84.5684.56 95.1695.16 99.2599.25 99.2599.25
对比例12Comparative Example 12 52.152.1 72.0472.04 82.6982.69 92.6492.64 99.6799.67 99.6699.66 99.6799.67 99.6899.68
对比例13Comparative Example 13 45.9645.96 67.2467.24 78.6978.69 91.6691.66 98.6598.65 99.8799.87 99.8799.87 99.8799.87
表4 水中的溶出度数据一览表Table 4 List of dissolution data in water
Figure PCTCN2021093201-appb-000003
Figure PCTCN2021093201-appb-000003
Figure PCTCN2021093201-appb-000004
Figure PCTCN2021093201-appb-000004
依据表2~4中溶出度的数据,绘制实施例1~6和对比例1~13制备的阿莫西林胶囊分别在pH4.0醋酸盐缓冲液、pH6.8磷酸盐缓冲液和水中的溶出度曲线图,具体参见图1~12。According to the dissolution data in Tables 2-4, the amoxicillin capsules prepared in Examples 1-6 and Comparative Examples 1-13 were drawn in pH4.0 acetate buffer, pH6.8 phosphate buffer and water, respectively. For the dissolution profiles, see Figures 1-12 for details.
由表2~4及图1~12可以看出,实施例1~6制备的阿莫西林胶囊的溶出度明显优于对比例1~13,说明本发明制备的阿莫西林胶囊在不同介质中都具有良好的溶出度。It can be seen from Tables 2 to 4 and Figures 1 to 12 that the dissolution rate of the amoxicillin capsules prepared in Examples 1 to 6 is significantly better than that of Comparative Examples 1 to 13, indicating that the amoxicillin capsules prepared by the present invention are in different media. All have good dissolution.
实验例2 阿莫西林胶囊的稳定性测定Experimental Example 2 Stability determination of amoxicillin capsules
取实施例1~6和对比例1~13中制得的阿莫西林胶囊(规格0.5g),分别于40±2℃、RH75±5%的条件下放置6个月,期间于第1、2、3和6个月取样,按稳定性检查项目检测,并与0天数据比较。Take the amoxicillin capsules (specification 0.5g) prepared in Examples 1 to 6 and Comparative Examples 1 to 13, and place them for 6 months under the conditions of 40±2° C. and RH75±5% respectively. Sampling at 2, 3 and 6 months, tested according to the stability check items, and compared with the 0-day data.
按照《中国药典》2015版中规定的样品含量、水分、有关物质、溶出度等指标及测定方法,对阿莫西林胶囊进行检测,具体检测结果见下表:Amoxicillin Capsules were tested in accordance with the indicators and determination methods of sample content, moisture, related substances, dissolution rate, etc. stipulated in the 2015 edition of the Chinese Pharmacopoeia. The specific test results are shown in the following table:
表5 稳定性检测结果一览表Table 5 List of stability test results
Figure PCTCN2021093201-appb-000005
Figure PCTCN2021093201-appb-000005
Figure PCTCN2021093201-appb-000006
Figure PCTCN2021093201-appb-000006
Figure PCTCN2021093201-appb-000007
Figure PCTCN2021093201-appb-000007
Figure PCTCN2021093201-appb-000008
Figure PCTCN2021093201-appb-000008
由表5可以看出,对比例1~13制备的阿莫西林胶囊不能同时兼具良好的溶出度和稳定性,且有关物质含量较高,而本发明实施例1~6制得的阿莫西林胶囊则具有良好的稳定性和溶出度,且有关物质含量较低。上述实验说明,本发明在制备阿莫西林胶囊过程中产生的杂质更少,更利于阿莫西林胶囊的制备和储存。As can be seen from Table 5, the amoxicillin capsules prepared in Comparative Examples 1-13 cannot have both good dissolution and stability at the same time, and the content of related substances is relatively high, while the amoxicillin capsules prepared in Examples 1-6 of the present invention Xilin capsules have good stability and dissolution, and the content of related substances is low. The above experiments show that the present invention produces less impurities in the process of preparing amoxicillin capsules, which is more conducive to the preparation and storage of amoxicillin capsules.
综上所述,本发明制备的阿莫西林胶囊能够同时兼具良好的溶出度及稳定性,且有关物质含量较低。To sum up, the amoxicillin capsules prepared by the present invention can have both good dissolution and stability, and the content of related substances is low.
显然,所描述的实施例仅仅是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。Obviously, the described embodiments are only some, but not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

Claims (10)

  1. 一种阿莫西林胶囊,其特征在于,制成它的有效成分的原料,包括:100重量份的阿莫西林药粉和0.2~0.5重量份硬脂酸镁;An amoxicillin capsule, characterized in that the raw materials for making its active ingredients include: 100 parts by weight of amoxicillin medicinal powder and 0.2-0.5 parts by weight of magnesium stearate;
    所述阿莫西林药粉是由10~35wt%粒度小于0.180mm的阿莫西林轻粉、10~40wt%粒度为0.600~0.850mm的阿莫西林重粉和余量的粒度为0.180~0.600mm的阿莫西林重粉组成。The amoxicillin medicinal powder is composed of 10-35wt% amoxicillin light powder with a particle size of less than 0.180mm, 10-40wt% amoxicillin heavy powder with a particle size of 0.600-0.850mm, and the remainder with a particle size of 0.180-0.600mm Amoxicillin heavy powder composition.
  2. 根据权利要求1所述的阿莫西林胶囊,其特征在于,所述阿莫西林药粉是使用压辊压力为6.0~10.0MPa的干法制粒机制得。The amoxicillin capsule according to claim 1, wherein the amoxicillin medicinal powder is prepared by using a dry granulator with a roller pressure of 6.0-10.0 MPa.
  3. 根据权利要求2所述的阿莫西林胶囊,其特征在于,在所述干法制粒机制粒过程中,环境湿度为52~58%。The amoxicillin capsule according to claim 2, wherein in the granulation process of the dry granulator, the ambient humidity is 52-58%.
  4. 根据权利要求2或3所述的阿莫西林胶囊,其特征在于,所述干法制粒机的工艺参数为:搅拌转速为15~20rpm,螺旋送料转速为50~60rpm,压辊转速为10~15rpm,压辊温度为20~30℃,整粒转速为100~130rpm,整粒筛网孔径为0.80~0.84mm,旋振筛筛网目数为20目、30目和80目。The amoxicillin capsule according to claim 2 or 3, wherein the technological parameters of the dry granulator are: the stirring speed is 15~20rpm, the screw feeding speed is 50~60rpm, and the pressing roller speed is 10~20rpm 15rpm, the temperature of the pressing roller is 20~30℃, the granulation speed is 100~130rpm, the granulation screen aperture is 0.80~0.84mm, and the mesh number of the rotary vibrating screen is 20 mesh, 30 mesh and 80 mesh.
  5. 根据权利要求1-3中任一项所述的阿莫西林胶囊,其特征在于,硬脂酸镁的粒度为0.180~0.850mm。The amoxicillin capsule according to any one of claims 1-3, wherein the granularity of magnesium stearate is 0.180-0.850 mm.
  6. 权利要求1-5中任一项所述的阿莫西林胶囊的制备方法,其特征在于,所述制备方法是取阿莫西林药粉经重粉混合后,再与硬脂酸镁交替投料进行混料,然后经充填及抛光,即得所述阿莫西林胶囊。The preparation method of the amoxicillin capsule described in any one of claims 1-5, it is characterised in that the preparation method is to take the amoxicillin medicinal powder and mix with the heavy powder, and then mix with magnesium stearate alternately for feeding After filling and polishing, the amoxicillin capsules are obtained.
  7. 根据权利要求6所述的阿莫西林胶囊的制备方法,其特征在于,所述重粉混合和混料的湿度均为52~58%。The method for preparing amoxicillin capsules according to claim 6, wherein the humidity of the heavy powder mixing and the mixing is 52-58%.
  8. 根据权利要求6或7所述的阿莫西林胶囊的制备方法,其特征在于,所述重粉混合的转速为12~15r/min、时间为11~15min;所述混料的转速为 12~15r/min、时间为2~5min。The method for preparing amoxicillin capsules according to claim 6 or 7, wherein the mixing speed of the heavy powder is 12-15 r/min and the time is 11-15 min; the mixing speed is 12-15 min. 15r/min, time is 2~5min.
  9. 根据权利要求6或7所述的阿莫西林胶囊的制备方法,其特征在于,所述重粉混合停止后,所得阿莫西林粉需静置5~10min,再取出与硬脂酸镁进行交替投料。The method for preparing amoxicillin capsules according to claim 6 or 7, characterized in that, after the heavy powder mixing is stopped, the obtained amoxicillin powder needs to stand for 5 to 10 minutes, and then take out and alternate with magnesium stearate. Feeding.
  10. 根据权利要求6或7所述的阿莫西林胶囊的制备方法,其特征在于,所述充填及抛光的湿度均为30~43%。The preparation method of amoxicillin capsules according to claim 6 or 7, characterized in that, the humidity of the filling and polishing is both 30-43%.
PCT/CN2021/093201 2021-04-21 2021-05-12 Amoxicillin capsule and preparation method therefor WO2022222205A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202110429386.8 2021-04-21
CN202110429386.8A CN113133986A (en) 2021-04-21 2021-04-21 Amoxicillin capsule and preparation method thereof

Publications (1)

Publication Number Publication Date
WO2022222205A1 true WO2022222205A1 (en) 2022-10-27

Family

ID=76813379

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2021/093201 WO2022222205A1 (en) 2021-04-21 2021-05-12 Amoxicillin capsule and preparation method therefor

Country Status (2)

Country Link
CN (1) CN113133986A (en)
WO (1) WO2022222205A1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107875136A (en) * 2017-12-27 2018-04-06 广州白云山医药集团股份有限公司白云山制药总厂 A kind of Amoxicillin pharmaceutical preparation and preparation method thereof
CN109172539A (en) * 2018-10-26 2019-01-11 海口市制药厂有限公司 A kind of Biomox and its production method and application
CN109908104A (en) * 2019-04-23 2019-06-21 石药集团中诺药业(石家庄)有限公司 A kind of amoxil capsule and preparation method thereof
CN109953971A (en) * 2019-05-14 2019-07-02 吉林市吴太感康药业有限公司 A kind of preparation method of amoxil capsule

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104856972B (en) * 2015-03-27 2018-03-27 华北制药股份有限公司 Amoxil capsule and preparation method thereof
CN108210475A (en) * 2016-12-13 2018-06-29 河南后羿实业集团有限公司 A kind of amoxil capsule and preparation method thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107875136A (en) * 2017-12-27 2018-04-06 广州白云山医药集团股份有限公司白云山制药总厂 A kind of Amoxicillin pharmaceutical preparation and preparation method thereof
CN109172539A (en) * 2018-10-26 2019-01-11 海口市制药厂有限公司 A kind of Biomox and its production method and application
CN109908104A (en) * 2019-04-23 2019-06-21 石药集团中诺药业(石家庄)有限公司 A kind of amoxil capsule and preparation method thereof
CN109953971A (en) * 2019-05-14 2019-07-02 吉林市吴太感康药业有限公司 A kind of preparation method of amoxil capsule

Also Published As

Publication number Publication date
CN113133986A (en) 2021-07-20

Similar Documents

Publication Publication Date Title
CN110650730B (en) Vitamin D analogue preparation and preparation method thereof
CN1156461C (en) Improved aqueous solubility pharmaceutical formulations
US20100247665A1 (en) Spherical Particle and Method for Producing the Same
EP2902015B1 (en) Preparation method of agomelatine solid preparation
WO2022222205A1 (en) Amoxicillin capsule and preparation method therefor
CN113648327A (en) A pharmaceutical composition containing sodium picosulfate, magnesium oxide, citric acid and/or potassium bicarbonate, and its preparation method
CN104688743B (en) Cefprozil suspension and preparation method thereof
CN113662919B (en) Stable cefixime tablet and preparation method thereof
CN107375231B (en) Preparation method of Olaparib composition capsule
CN110123770A (en) A kind of Eliquis pharmaceutical composition and preparation method thereof
CN111346064B (en) Rivaroxaban tablet and preparation method thereof
CN114366757A (en) Compound polyethylene glycol electrolyte and preparation method thereof
CN110840848A (en) Racecadotril granules and preparation method thereof
CN108853030B (en) Medicinal preparation for treating malignant tumor and preparation method thereof
CN113616613A (en) Metformin-glipizide compound tablet for treating diabetes and preparation method thereof
JPH05105636A (en) Antacid agent composition
CN106692149A (en) Cariprazine medical oral preparation and preparation method thereof
CN85101689A (en) Nifedipine preparation and preparation method thereof
CN115381834B (en) Ticagrelor slow-release solid composition and capsule preparation containing same
CN1839835A (en) Lacidipine pharmaceutical formulation preparing method
CN115154456B (en) Pharmaceutical composition of metformin and enggliflozin and preparation method thereof
CN115212171B (en) Ticagrelor sustained-release pellet and pharmaceutical preparation containing same
CN112535674B (en) Letrozole tablet and preparation method thereof
CN115444823B (en) Rebamipide-containing particles and preparation method and application thereof
CN108514550A (en) Solid drugs and preparation method thereof containing Abiraterone acetate

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 21937431

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 21937431

Country of ref document: EP

Kind code of ref document: A1