WO2017036140A1 - A-group neisseria meningitidis cultivation method - Google Patents

A-group neisseria meningitidis cultivation method Download PDF

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WO2017036140A1
WO2017036140A1 PCT/CN2016/078086 CN2016078086W WO2017036140A1 WO 2017036140 A1 WO2017036140 A1 WO 2017036140A1 CN 2016078086 W CN2016078086 W CN 2016078086W WO 2017036140 A1 WO2017036140 A1 WO 2017036140A1
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culture
bacteria
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朱冲
米强
陈道远
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成都欧林生物科技股份有限公司
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    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
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    • C12R2001/36Neisseria

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  • the present invention relates to a method for cultivating a strain, and particularly relates to a method for culturing a group A meningococcus.
  • ECM epidemic cerebrospinal meningitis
  • Neisseria mening gitidis is an acute respiratory infection caused by Neisseria mening gitidis.
  • the susceptible population is mainly children, with the highest rate of fulminant deaths, up to 40 ⁇ 3 ⁇ 4 ⁇ 60 ⁇ 3 ⁇ 4.
  • the incidence rate in every continent in the world is between 1/100,000 and 10/10 million, and the total case fatality rate is 5% ⁇ 15 ⁇ 3 ⁇ 4.
  • Up to 20% of meningitis patients have neurological sequelae, including mental impairment and deafness.
  • Serological classification according to the capsular polysaccharide type can be divided into 13 serotypes, of which group A, group B, and group C account for about 90% of the epidemic group.
  • Group A meningococcal is a major epidemic of the major pathogenic serogroups, especially in the so-called African “Brain Brain Epidemic Belt”, which is a major epidemic every 7-14 years.
  • the most effective way to prevent epidemic cerebrospinal meningitis is to vaccinate.
  • the meningococcal polysaccharide vaccine currently included in the national immunization program includes group A meningococcal polysaccharide vaccine, group A group C meningococcal polysaccharide vaccine.
  • polysaccharides are extracted from group A meningococcus to form a polysaccharide vaccine, thereby achieving the effect of preventing meningitis. Because the polysaccharide is extracted from the capsule, if there are more dead bacteria in the culture process of the strain, it is easy to cause the extraction efficiency of the polysaccharide extracted directly from the group A meningococcus is low, and the extracted polysaccharide is not Easy to purify.
  • the object of the present invention is to solve the problem that the extraction efficiency of the polysaccharide extracted directly from group A meningococcus is low in the prior art, and the extracted polysaccharide is not easy to be purified, and a group A meningitis which solves the above problems is provided. Method of cultivating cocci.
  • a method for culturing group A meningococcus includes the following steps:
  • the seed for production is inoculated into the fermenter for 6 to 12 hours; the medium in the fermenter is a semi-integrated medium, the temperature is 35 to 37 ° C, and the pH of the medium is 7.0 to 7.2.
  • the stirring speed in the fermenter was 140 to 1 50 r/min, and the inoculum amount was 10 to 150,000/ml.
  • step (1) is as follows:
  • a group of N. meningitidis strains were inoculated on a purification medium, and incubated at 38 ° C for 20 h, and the robust and no-bacteria-contaminated strains were selected and then inoculated onto the purification medium for secondary treatment.
  • the culture was incubated at 38 ° C for 12 h, and the strains with strong and no fungus contamination were selected and added to the sterile skim milk, and the purified working seed strains were prepared by mixing and lyophilizing.
  • the process of purifying the purified seed is as follows:
  • step (2) is as follows:
  • the purified seed after inoculation is inoculated into a semi-integrated liquid medium for activation culture; the conditions of the activation culture are temperature 35 to 37 ° C, pH 7.0 to 7.2, stirring speed 140 to 150 r / min, culture ⁇ The interval is 6 ⁇ 8h; finally, the activated purified seeds are cultured in three generations to prepare a suitable number of production seeds.
  • the conditions for the three-generation expansion culture are: the culture medium for expansion culture is a semi-integrated liquid medium; the incubation conditions are temperature 35 to 37 ° C, pH 7.0 to 7.2, stirring speed 140 ⁇ 150r/min.
  • composition of the semi-integrated liquid medium is as follows:
  • the group A meningococcal bacteria cultivated by the invention have fewer dead bacteria, and the extracted polysaccharide is more easily purified; and the extraction rate of the polysaccharide in the capsule is higher.
  • a method for culturing group A meningococcus comprises the following steps:
  • [1] Preparation of purified working seed strains: Inoculating Group A N. meningitidis strains onto a purification medium, culturing at 38 ° C for 20 hours, selecting robust and non-organic contamination The strain is inoculated on the purification medium for secondary culture, and then incubated at 38 ° C for 12 h. The robust and bacteria-free bacteria are added to the sterile skim milk, and the mixture is lyophilized to obtain purified. Working seed strains.
  • the purified seed after inoculation is inoculated into a semi-integrated liquid medium for activation culture; the conditions of the activation culture are temperature 35 to 37 ° C, pH 7.0 to 7.2, stirring speed 140 to 150 r/min, and culture ⁇ The interval is 6 ⁇ 8h;
  • the activated purified seed is subjected to three generations of expansion culture to prepare a suitable amount of production seeds; wherein the medium for expansion culture is semi-integrated liquid medium; the cultivation condition is temperature 35 to 37 ° C , p H7.0 ⁇ 7.2, stirring speed 140 ⁇ 150r/min.
  • the specific cultivation conditions in each step are as follows:
  • Step (2) The working condition of the seed strain is 35 ° C, and the culture is carried out for 18 hours; the conditions of the activation culture are the temperature of 37 ° C, the pH of 7.2, the stirring speed of 140 r / min, and the cultivation of the daytime. 6 ⁇ 8h; the incubation conditions for the expansion culture are temperature 36 ° C, pH 7.0, stirring speed 145r / min;
  • the fermentation condition of the fermenter culture in the step (3) is a temperature of 37 ° C, a pH of the medium of 7.0, a stirring speed of 145 r / min, and an inoculum amount of 120,000 / ml.
  • the purification medium used in the step (1) is a chocolate medium added with an antibiotic, which is effective for the purpose of purification;
  • the medium used in the step (2) of the seed seed strain is the chocolate without antibiotic added.
  • the medium that is, 10% sheep blood agar medium, can effectively achieve the effect of the seed strain of the seed by the culture of the medium.
  • the medium used for the culture for activation and amplification is a semi-integrated liquid medium, and the ratio of the medium is: beef leachate 1 L, peptone 10 g, sodium chloride 5 g, sterile defibrinated horse blood, sheep blood Or rabbit blood 100ml, glucose 3g, hydrochloric acid casein hydrolysate 2g, pH 7.0 ⁇ 7.2.
  • Step (2) The working seed culture strain is cultured at 36 ° C, and cultured for 16 hours; the conditions of activation culture are temperature 37 ° C, pH 7.0, stirring speed 145 r / min, culture daytime 8h; the cultivation conditions for the amplification culture are temperature 37 ° C, pH 7.0, stirring speed 150 r / min;
  • the culture condition of the fermenter culture in the step (3) is a temperature of 37 ° C, a pH of the medium of 7.0, a stirring speed of 150 r / min, and an inoculum amount of 150,000 / ml.
  • Step (2) The working condition of the seed strain is 37 ° C, and the culture is carried out for 18 hours; the conditions of the activation culture are the temperature of 36 ° C, the pH of 7.2, the stirring speed of 150 r / min, and the cultivation of the daytime. 7h; cultivation of expansion culture The conditions are temperature 37 ° C, pH 7.2, stirring speed 145 r / min;
  • the fermentation condition of the fermenter culture in the step (3) is a temperature of 37 ° C, a pH of the medium of 7.2, a stirring speed of 145 r / min, and an inoculum amount of 100,000 / ml.

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Abstract

An A-group Neisseria meningitidis cultivation method comprises the following steps: (1) preparing purified strains of a working seed lot; (2) opening the strains of the working seed lot, inoculating same into a semi-synthetic culture medium, performing cultivation at the temperature of 35-37°C for 16-24 hours, and then preparing an appropriate quantity of seeds for production after three-generation multiplication culture; and (3) inoculating the seeds for production into a fermentation tank, and performing cultivation for 6-12 hours, the culture medium in the fermentation tank being a semi-synthetic culture medium, the temperature being 35-37°C, the pH of the culture medium being 7.0-7.2, the stirring speed in the fermentation tank being 140-150 r/min, and the inoculation quantity being 100,000 ml to 150,000 ml.

Description

说明书 发明名称: A群脑膜炎球菌的培养方法 技术领域  Specification Name of Invention: Method for culturing group A meningococcal bacteria
[0001] 本发明涉及一种菌种的培养方法, 具体涉及的是 A群脑膜炎球菌的培养方法。  [0001] The present invention relates to a method for cultivating a strain, and particularly relates to a method for culturing a group A meningococcus.
背景技术  Background technique
[0002] 流行性脑脊髓膜炎 (简称流脑, 下同)是一种由奈瑟氏脑膜炎球菌 (Neisseriamenin gitidis)引起的急性呼吸道传染病。 一百多年来, 一直在世界各地流行或散在发生 , 感染病原菌后可引起败血症、 脑膜炎。 易感人群主要为儿童, 以暴发型病死 率最高, 可达 40<¾〜60<¾。 当今世界各大洲发病率在 1/10万〜 10/10万, 总病死率 在 5%〜15<¾, 高达 20%的脑膜炎患者会有神经系统后遗症, 包括智力受损和耳 聋等。 根据荚膜多糖型别进行血清学分类可分 13个血清型, 其中 A群、 B群、 C 群约占流行菌群的 90%。 A群脑膜炎球菌是较大流行的主要致病血清群, 特别是 在所谓的非洲 "流脑流行带", 每隔 7-14年就会出现一次较大流行。  [0002] Epidemic cerebrospinal meningitis (abbreviated as ECM, the same below) is an acute respiratory infection caused by Neisseria mening gitidis. For more than 100 years, it has been prevalent or scattered around the world, causing sepsis and meningitis after infection with pathogens. The susceptible population is mainly children, with the highest rate of fulminant deaths, up to 40<3⁄4~60<3⁄4. The incidence rate in every continent in the world is between 1/100,000 and 10/10 million, and the total case fatality rate is 5%~15<3⁄4. Up to 20% of meningitis patients have neurological sequelae, including mental impairment and deafness. Serological classification according to the capsular polysaccharide type can be divided into 13 serotypes, of which group A, group B, and group C account for about 90% of the epidemic group. Group A meningococcal is a major epidemic of the major pathogenic serogroups, especially in the so-called African “Brain Brain Epidemic Belt”, which is a major epidemic every 7-14 years.
[0003] 我国于 1938年、 1949年、 1959年、 1967年和 1977年曾发生过 5次全国性流脑流 行; 其中以 1967年春季流行最为严重, 发病率高达 403/10万, 病死率为 5.49<¾。 我国过去 90%以上的病例是 A群病菌致病, 现在 B群或 C群病菌有吋亦弓 I起流脑暴 发。 2003年幵始, C群流脑的发病率明显上升。 目前 A群和 C群共占所有血清群 的 50%以上, 且 C群仍有进一步增高的趋势。 因此, 目前我国预防流脑工作的重 点是以预防 A群和 C群为主。  [0003] There were five national epidemic epidemics in China in 1938, 1949, 1959, 1967, and 1977; among them, the most prevalent in the spring of 1967, the incidence rate was as high as 403/100,000, and the mortality rate was 5.49<3⁄4. In the past 90% of cases in China, the disease of group A was caused by disease. Now, group B or group C germs have convulsions. Since the beginning of 2003, the incidence of C group cerebral palsy has increased significantly. At present, group A and group C account for more than 50% of all serogroups, and group C still has a tendency to increase further. Therefore, the focus of prevention of epidemic work in China is to prevent group A and group C.
[0004] 目前预防流行性脑脊髓膜炎最有效的方法是接种疫苗。 研究表明, A群 C群脑 膜炎球菌的荚膜多糖具有良好的免疫原性, 提取荚膜多糖可直接制备成疫苗, 经注射免疫后的人群可以获得免疫保护。 我国从 2007年起已将流脑疫苗纳入国 家免疫规划, 在全国范围对适齢儿童普及接种。 目前纳入国家免疫计划的流脑 多糖疫苗包括 A群脑膜炎球菌多糖疫苗, A群 C群脑膜炎球菌多糖疫苗。  [0004] The most effective way to prevent epidemic cerebrospinal meningitis is to vaccinate. Studies have shown that the capsular polysaccharide of group A group C meningococcus has good immunogenicity, and the capsular polysaccharide can be directly prepared into a vaccine, and the immunized population can obtain immune protection. Since 2007, China has included meningococcal vaccines into national immunization programs, and has universally vaccinated suitable children across the country. The meningococcal polysaccharide vaccine currently included in the national immunization program includes group A meningococcal polysaccharide vaccine, group A group C meningococcal polysaccharide vaccine.
[0005] 现有技术中均是从 A群脑膜炎球菌中提取出多糖制成多糖疫苗, 进而达到预防 脑膜炎的效果。 因多糖是从荚膜中提取出来, 如果菌种培养过程中死菌较多, 容易导致直接从 A群脑膜炎球菌中提取多糖的提取效率低, 且提取出来的多糖不 容易纯化。 [0005] In the prior art, polysaccharides are extracted from group A meningococcus to form a polysaccharide vaccine, thereby achieving the effect of preventing meningitis. Because the polysaccharide is extracted from the capsule, if there are more dead bacteria in the culture process of the strain, it is easy to cause the extraction efficiency of the polysaccharide extracted directly from the group A meningococcus is low, and the extracted polysaccharide is not Easy to purify.
技术问题  technical problem
[0006] 本发明的目的在于解决现有技术中直接从 A群脑膜炎球菌中提取多糖的提取效 率低, 且提取出来的多糖不容易纯化的问题, 提供一种解决上述问题的 A群脑膜 炎球菌的培养方法。  [0006] The object of the present invention is to solve the problem that the extraction efficiency of the polysaccharide extracted directly from group A meningococcus is low in the prior art, and the extracted polysaccharide is not easy to be purified, and a group A meningitis which solves the above problems is provided. Method of cultivating cocci.
问题的解决方案  Problem solution
技术解决方案  Technical solution
[0007] 为解决上述缺点, 本发明的技术方案如下: [0007] In order to solve the above disadvantages, the technical solution of the present invention is as follows:
[0008] A群脑膜炎球菌的培养方法, 包括以下步骤: [0008] A method for culturing group A meningococcus includes the following steps:
[0009] (1) 制备纯化的工作种子批菌种; [0009] (1) preparing a purified working seed strain;
[0010] (2) 幵启工作种子批菌种, 接种至半综合培养基中, 在温度 35〜37°C条件下 培养 16〜24小吋, 然后经过三代扩增培养, 制备数量适宜的生产用种子;  [0010] (2) 工作 工作 working seed batch strain, inoculated into semi-integrated medium, cultured at a temperature of 35~37 ° C for 16~24 吋, and then three-generation expansion culture to prepare a suitable amount of production Seed
[0011] (3) 将生产用种子接种至发酵罐培养 6〜12小吋即可; 发酵罐中培养基为半综 合培养基, 温度为 35〜37°C, 培养基 pH为 7.0〜7.2, 发酵罐中搅拌速度为 140〜1 50r/min, 接种量为 10〜15万 /ml。  [0011] (3) The seed for production is inoculated into the fermenter for 6 to 12 hours; the medium in the fermenter is a semi-integrated medium, the temperature is 35 to 37 ° C, and the pH of the medium is 7.0 to 7.2. The stirring speed in the fermenter was 140 to 1 50 r/min, and the inoculum amount was 10 to 150,000/ml.
[0012] 优选地, 所述步骤 (1) 的具体过程如下:  [0012] Preferably, the specific process of the step (1) is as follows:
[0013] 将 A群脑膜炎奈瑟氏球菌菌种接种到纯化培养基上, 在 38°C条件下培育 20h, 挑 选健壮且无杂菌污染的菌种再接种到纯化培养基上进行二次培养, 再在 38°C条件 下培育 12h, 挑选健壮且无杂菌污染的菌种加入无菌脱脂牛奶中, 混匀冻干制备 即得纯化的工作种子批菌种。  [0013] A group of N. meningitidis strains were inoculated on a purification medium, and incubated at 38 ° C for 20 h, and the robust and no-bacteria-contaminated strains were selected and then inoculated onto the purification medium for secondary treatment. The culture was incubated at 38 ° C for 12 h, and the strains with strong and no fungus contamination were selected and added to the sterile skim milk, and the purified working seed strains were prepared by mixing and lyophilizing.
[0014] 作为优选的实施方式, 所述纯化种子的幵启过程如下:  [0014] As a preferred embodiment, the process of purifying the purified seed is as follows:
[0015] 将工作种子批菌种溶解到无菌水中, 将其接种在 10%羊血琼脂培养基上, 放于  [0015] Dissolving the working seed strain in sterile water, inoculation on 10% sheep blood agar medium, and placing
35〜37°C的环境下培养 16〜20小吋后, 挑选出健壮且无杂菌污染的菌种即可。  After culturing for 16 to 20 hours in an environment of 35 to 37 ° C, select a strain that is robust and free of contamination by bacteria.
[0016] 进一步, 所述步骤 (2) 的具体培育过程如下: [0016] Further, the specific cultivation process of the step (2) is as follows:
[0017] 将幵启后的纯化种子接种到半综合液体培养基中进行活化培养; 活化培养的条 件为温度 35〜37°C、 pH7.0〜7.2、 搅拌速度 140〜150r/min, 培养吋间为 6〜8h; 最后将活化后的纯化种子经过三代扩增培养, 即可制备数量适宜的生产用种子 [0018] 更进一步地, 所述三代扩增培养的条件为: 扩增培养用培养基为半综合液体培 养基中; 培育条件为温度 35〜37°C、 pH7.0〜7.2、 搅拌速度 140〜150r/min。 [0017] The purified seed after inoculation is inoculated into a semi-integrated liquid medium for activation culture; the conditions of the activation culture are temperature 35 to 37 ° C, pH 7.0 to 7.2, stirring speed 140 to 150 r / min, culture 吋The interval is 6~8h; finally, the activated purified seeds are cultured in three generations to prepare a suitable number of production seeds. [0018] Further, the conditions for the three-generation expansion culture are: the culture medium for expansion culture is a semi-integrated liquid medium; the incubation conditions are temperature 35 to 37 ° C, pH 7.0 to 7.2, stirring speed 140 ~150r/min.
[0019] 为了达到最好的效果, 所述半综合液体培养基的组成配比如下: [0019] In order to achieve the best results, the composition of the semi-integrated liquid medium is as follows:
[0020] 牛肉浸出液 1L, 蛋白胨 10g, 氯化钠 5g, 无菌脱纤维马血、 羊血或兔血 100ml, 葡萄糖 3g, 盐酸酪蛋白水解物 2g, pH7.0〜7.2。 [0020] Beef leachate 1L, peptone 10g, sodium chloride 5g, sterile defibrinated horse blood, sheep blood or rabbit blood 100ml, glucose 3g, hydrochloric acid casein hydrolysate 2g, pH 7.0~7.2.
发明的有益效果  Advantageous effects of the invention
有益效果  Beneficial effect
[0021] 本发明与现有技术相比, 具有以下优点及有益效果:  [0021] Compared with the prior art, the present invention has the following advantages and beneficial effects:
[0022] 本发明培育出的 A群脑膜炎球菌的死菌较少, 提取出的多糖纯化更加容易; 而 且多糖在荚膜中的提取率更高。  [0022] The group A meningococcal bacteria cultivated by the invention have fewer dead bacteria, and the extracted polysaccharide is more easily purified; and the extraction rate of the polysaccharide in the capsule is higher.
本发明的实施方式 Embodiments of the invention
[0023] 下面结合实施例, 对本发明作进一步地详细说明, 但本发明的实施方式不限于 此。  The present invention will be further described in detail below with reference to the embodiments, but the embodiments of the present invention are not limited thereto.
[0024] 实施例 1  Embodiment 1
[0025] A群脑膜炎球菌的培养方法, 包括以下步骤:  [0025] A method for culturing group A meningococcus comprises the following steps:
[0026] (1) 制备纯化的工作种子批菌种: 将 A群脑膜炎奈瑟氏球菌菌种接种到纯化培 养基上, 在 38°C条件下培育 20h, 挑选健壮且无杂菌污染的菌种再接种到纯化培 养基上进行二次培养, 再在 38°C条件下培育 12h, 挑选健壮且无杂菌污染的菌种 加入无菌脱脂牛奶中, 混匀冻干制备即得纯化的工作种子批菌种。  [1] (1) Preparation of purified working seed strains: Inoculating Group A N. meningitidis strains onto a purification medium, culturing at 38 ° C for 20 hours, selecting robust and non-organic contamination The strain is inoculated on the purification medium for secondary culture, and then incubated at 38 ° C for 12 h. The robust and bacteria-free bacteria are added to the sterile skim milk, and the mixture is lyophilized to obtain purified. Working seed strains.
[0027] (2) 将工作种子批菌种溶解到无菌水中, 将其接种在 10%羊血琼脂培养基上 , 放于 35〜37°C的环境下培养 16〜20小吋后, 挑选出健壮且无杂菌污染的菌种; [0027] (2) Dissolving the working seed strain in sterile water, inoculation on 10% sheep blood agar medium, and culturing in the environment of 35~37 ° C for 16~20 hours, then selecting a robust and no-bacteria-contaminated strain;
[0028] 将幵启后的纯化种子接种到半综合液体培养基中进行活化培养; 活化培养的条 件为温度 35〜37°C、 pH7.0〜7.2、 搅拌速度 140〜150r/min, 培养吋间为 6〜8h; [0028] The purified seed after inoculation is inoculated into a semi-integrated liquid medium for activation culture; the conditions of the activation culture are temperature 35 to 37 ° C, pH 7.0 to 7.2, stirring speed 140 to 150 r/min, and culture 吋The interval is 6~8h;
[0029] 最后将活化后的纯化种子经过三代扩增培养, 即可制备数量适宜的生产用种子 ; 其中扩增培养用培养基为半综合液体培养基中; 培育条件为温度 35〜37°C、 p H7.0〜7.2、 搅拌速度 140〜150r/min。  [0029] Finally, the activated purified seed is subjected to three generations of expansion culture to prepare a suitable amount of production seeds; wherein the medium for expansion culture is semi-integrated liquid medium; the cultivation condition is temperature 35 to 37 ° C , p H7.0~7.2, stirring speed 140~150r/min.
[0030] (3) 将生产用种子接种至发酵罐培养 6〜12小吋即可; 发酵罐中培养基为半综 合培养基, 温度为 35〜37°C, 培养基 pH为 7.0〜7.2, 发酵罐中搅拌速度为 140〜1 50r/min, 接种量为 10〜15万 /ml。 [0030] (3) inoculating the production seed into the fermenter for 6 to 12 hours; the medium in the fermenter is semi-complex The medium is mixed at a temperature of 35 to 37 ° C, the pH of the medium is 7.0 to 7.2, the stirring speed in the fermenter is 140 to 1 50 r/min, and the inoculum is 10 to 150,000/ml.
[0031] 本实施例中, 各步骤中的具体培育条件如下: [0031] In this embodiment, the specific cultivation conditions in each step are as follows:
[0032] 步骤 (2) 工作种子批菌种幵启的培育条件为 35°C, 培养 18小吋; 活化培养的 条件为温度 37°C、 pH7.2、 搅拌速度 140r/min, 培养吋间为 6〜8h; 扩增培养的培 育条件为温度 36°C、 pH7.0、 搅拌速度 145r/min;  [0032] Step (2) The working condition of the seed strain is 35 ° C, and the culture is carried out for 18 hours; the conditions of the activation culture are the temperature of 37 ° C, the pH of 7.2, the stirring speed of 140 r / min, and the cultivation of the daytime. 6~8h; the incubation conditions for the expansion culture are temperature 36 ° C, pH 7.0, stirring speed 145r / min;
[0033] 步骤 (3) 中发酵罐培养的培育条件为温度为 37°C, 培养基 pH为 7.0, 搅拌速度 为 145r/min, 接种量为 12万 /ml。 [0033] The fermentation condition of the fermenter culture in the step (3) is a temperature of 37 ° C, a pH of the medium of 7.0, a stirring speed of 145 r / min, and an inoculum amount of 120,000 / ml.
[0034] 且步骤 (1) 中采用的纯化培养基为加入抗生素的巧克力培养基, 有效达到纯 化的目的; 步骤 (2) 中幵启工作种子批菌种所使用培养基为未加入抗生素的巧 克力培养基, 即 10%羊血琼脂培养基, 通过该培养基的培养后即可有效达到幵启 工作种子批菌种的效果。 [0034] and the purification medium used in the step (1) is a chocolate medium added with an antibiotic, which is effective for the purpose of purification; the medium used in the step (2) of the seed seed strain is the chocolate without antibiotic added. The medium, that is, 10% sheep blood agar medium, can effectively achieve the effect of the seed strain of the seed by the culture of the medium.
[0035] 活化和扩增用培养所用的培养基均是半综合液体培养基, 该培养基的配比为: 牛肉浸出液 1L, 蛋白胨 10g, 氯化钠 5g, 无菌脱纤维马血、 羊血或兔血 100ml, 葡萄糖 3g, 盐酸酪蛋白水解物 2g, pH7.0〜7.2。 [0035] The medium used for the culture for activation and amplification is a semi-integrated liquid medium, and the ratio of the medium is: beef leachate 1 L, peptone 10 g, sodium chloride 5 g, sterile defibrinated horse blood, sheep blood Or rabbit blood 100ml, glucose 3g, hydrochloric acid casein hydrolysate 2g, pH 7.0~7.2.
[0036] 实施例 2 Embodiment 2
[0037] 本实施例与实施例 1的区别仅仅在于, 各步骤中的具体培育条件不同, 具体设 置如下:  [0037] The difference between this embodiment and Embodiment 1 is only that the specific cultivation conditions in each step are different, and the specific settings are as follows:
[0038] 步骤 (2) 工作种子批菌种幵启的培育条件为 36°C, 培养 16小吋; 活化培养的 条件为温度 37°C、 pH7.0、 搅拌速度 145r/min, 培养吋间为 8h; 扩增培养的培育 条件为温度 37°C、 pH7.0、 搅拌速度 150r/min;  [0038] Step (2) The working seed culture strain is cultured at 36 ° C, and cultured for 16 hours; the conditions of activation culture are temperature 37 ° C, pH 7.0, stirring speed 145 r / min, culture daytime 8h; the cultivation conditions for the amplification culture are temperature 37 ° C, pH 7.0, stirring speed 150 r / min;
[0039] 步骤 (3) 中发酵罐培养的培育条件为温度为 37°C, 培养基 pH为 7.0, 搅拌速度 为 150r/min, 接种量为 15万 /ml。  [0039] The culture condition of the fermenter culture in the step (3) is a temperature of 37 ° C, a pH of the medium of 7.0, a stirring speed of 150 r / min, and an inoculum amount of 150,000 / ml.
[0040] 实施例 3  Embodiment 3
[0041] 本实施例与实施例 1的区别仅仅在于, 各步骤中的具体培育条件不同, 具体设 置如下:  [0041] The difference between this embodiment and Embodiment 1 is only that the specific cultivation conditions in each step are different, and the specific settings are as follows:
[0042] 步骤 (2) 工作种子批菌种幵启的培育条件为 37°C, 培养 18小吋; 活化培养的 条件为温度 36°C、 pH7.2、 搅拌速度 150r/min, 培养吋间为 7h; 扩增培养的培育 条件为温度 37°C、 pH7.2、 搅拌速度 145r/min; [0042] Step (2) The working condition of the seed strain is 37 ° C, and the culture is carried out for 18 hours; the conditions of the activation culture are the temperature of 36 ° C, the pH of 7.2, the stirring speed of 150 r / min, and the cultivation of the daytime. 7h; cultivation of expansion culture The conditions are temperature 37 ° C, pH 7.2, stirring speed 145 r / min;
[0043] 步骤 (3) 中发酵罐培养的培育条件为温度为 37°C, 培养基 pH为 7.2, 搅拌速度 为 145r/min, 接种量为 10万 /ml。 [0043] The fermentation condition of the fermenter culture in the step (3) is a temperature of 37 ° C, a pH of the medium of 7.2, a stirring speed of 145 r / min, and an inoculum amount of 100,000 / ml.
[0044] 上述实施例仅为本发明的优选实施例, 并非对本发明保护范围的限制, 但凡采 用本发明的设计原理, 以及在此基础上进行非创造性劳动而作出的变化, 均应 属于本发明的保护范围之内。 The above embodiments are merely preferred embodiments of the present invention, and are not intended to limit the scope of the present invention, and any changes made by the design principles of the present invention and non-inventive work on the basis of the present invention belong to the present invention. Within the scope of protection.

Claims

权利要求书 Claim
[权利要求 1] A群脑膜炎球菌的培养方法, 其特征在于, 包括以下步骤:  [Claim 1] A method for culturing a group A meningococcal strain, comprising the steps of:
(1) 制备纯化的工作种子批菌种;  (1) preparing a purified working seed strain;
(2) 幵启工作种子批菌种, 接种至半综合培养基中, 在温度 35〜37 °C条件下培养 16〜24小吋, 然后经过三代扩增培养, 制备数量适宜的 生产用种子;  (2) 工作 工作 working seed batch strain, inoculated into semi-integrated medium, cultured at a temperature of 35~37 °C for 16~24 hours, and then subjected to three generations of expansion culture to prepare a suitable amount of production seeds;
(3) 将生产用种子接种至发酵罐培养 6〜12小吋即可; 发酵罐中培养 基为半综合培养基, 温度为 35〜37°C, 培养基 pH为 7.0〜7.2, 发酵罐 中搅拌速度为 140〜150r/min, 接种量为 10〜15万 /ml。  (3) Inoculate the production seeds into the fermenter for 6~12 hours; the medium in the fermenter is semi-integrated medium, the temperature is 35~37°C, the medium pH is 7.0~7.2, in the fermenter The stirring speed was 140 to 150 r/min, and the inoculum amount was 10 to 150,000/ml.
2.根据权利要求 1所述的 A群脑膜炎球菌的培养方法, 其特征在于, 所述步骤 (1) 的具体过程如下:  The method for culturing a group A meningococcus according to claim 1, wherein the specific process of the step (1) is as follows:
将 A群脑膜炎奈瑟氏球菌菌种接种到纯化培养基上, 在 38°C条件下培 育 20h, 挑选健壮且无杂菌污染的菌种再接种到纯化培养基上进行二 次培养, 再在 38°C条件下培育 12h, 挑选健壮且无杂菌污染的菌种加 入无菌脱脂牛奶中, 混匀冻干制备即得纯化的工作种子批菌种。 A group of N. meningitidis strains were inoculated on the purification medium, and incubated at 38 ° C for 20 h. The robust and no-bacteria-contaminated strains were selected and then inoculated onto the purification medium for secondary culture. After incubating at 38 °C for 12 h, select the robust and bacteria-free bacteria into the sterile skim milk, and mix and freeze to prepare the purified working seed strain.
3.根据权利要求 1所述的 A群脑膜炎球菌的培养方法, 其特征在于, 所述纯化种子的幵启过程如下: The method for culturing group A meningococcus according to claim 1, wherein the process of purifying the seed is as follows:
将工作种子批菌种溶解到无菌水中, 将其接种在 10%羊血琼脂培养基 上, 放于 35〜37°C的环境下培养 16〜20小吋后, 挑选出健壮且无杂菌 污染的菌种即可。  The working seed batch is dissolved in sterile water, inoculated on 10% sheep blood agar medium, and cultured in the environment of 35~37 ° C for 16~20 hours, and then selected to be robust and free of bacteria. Contaminated bacteria can be used.
4.根据权利要求 3所述的 A群脑膜炎球菌的培养方法, 其特征在于, 所述步骤 (2) 的具体培育过程如下:  The method for culturing group A meningococcus according to claim 3, wherein the specific cultivation process of the step (2) is as follows:
将幵启后的纯化种子接种到半综合液体培养基中进行活化培养; 活化 培养的条件为温度 35〜37°C、 pH7.0〜7.2、 搅拌速度 140〜150r/min, 培养吋间为 6〜8h; 最后将活化后的纯化种子经过三代扩增培养, 即 可制备数量适宜的生产用种子。  The purified seeds after inoculation are inoculated into a semi-integrated liquid medium for activation culture; the conditions for activation culture are temperature 35 to 37 ° C, pH 7.0 to 7.2, stirring speed 140 to 150 r/min, and culture time is 6 ~8h; Finally, the activated purified seeds are subjected to three generations of expansion culture to prepare a suitable amount of production seeds.
5.根据权利要求 4所述的 A群脑膜炎球菌的培养方法, 其特征在于, 所述三代扩增培养的条件为: 扩增培养用培养基为半综合液体培养基 中; 培育条件为温度 35〜37°C、 pH7.0〜7.2、 搅拌速度 140〜150r/min The method for culturing group A meningococcal bacteria according to claim 4, wherein the conditions for the three-generation expansion culture are: the medium for expansion culture is a semi-integrated liquid medium Medium; incubation conditions are temperature 35~37 ° C, pH 7.0~7.2, stirring speed 140~150r/min
6.根据权利要求 1所述的 A群脑膜炎球菌的培养方法, 其特征在于, 所述半综合液体培养基的组成配比如下: The method for culturing group A meningococcal bacteria according to claim 1, wherein the composition of the semi-integrated liquid medium is as follows:
牛肉浸出液 1L, 蛋白胨 10g, 氯化钠 5g, 无菌脱纤维马血、 羊血或兔 血 100ml, 葡萄糖 3g, 盐酸酪蛋白水解物 2g, pH7.0〜7.2。 Beef leachate 1L, peptone 10g, sodium chloride 5g, sterile defibrinated horse blood, sheep blood or rabbit blood 100ml, glucose 3g, hydrochloric acid casein hydrolysate 2g, pH 7.0~7.2.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102327605A (en) * 2011-08-25 2012-01-25 成都康华生物制品有限公司 Preparation process of meningococcal polysaccharide vaccine
CN103721249A (en) * 2014-01-16 2014-04-16 华兰生物工程股份有限公司 Meningitis vaccine and preparation method thereof
CN104689309A (en) * 2015-03-27 2015-06-10 成都欧林生物科技股份有限公司 Separated and purified acellular pertussis-diphtheria-tetanus, b-type haemophilus influenzae and A-group and C-group meningococcus combined vaccine and preparation method thereof
CN105039227A (en) * 2015-08-31 2015-11-11 成都欧林生物科技股份有限公司 A-group Neisseria meningitidis cultivation method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102327605A (en) * 2011-08-25 2012-01-25 成都康华生物制品有限公司 Preparation process of meningococcal polysaccharide vaccine
CN103721249A (en) * 2014-01-16 2014-04-16 华兰生物工程股份有限公司 Meningitis vaccine and preparation method thereof
CN104689309A (en) * 2015-03-27 2015-06-10 成都欧林生物科技股份有限公司 Separated and purified acellular pertussis-diphtheria-tetanus, b-type haemophilus influenzae and A-group and C-group meningococcus combined vaccine and preparation method thereof
CN105039227A (en) * 2015-08-31 2015-11-11 成都欧林生物科技股份有限公司 A-group Neisseria meningitidis cultivation method

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