WO2017012570A1 - Bacillus coagulans, high cell density fermentation method thereof, and method for preparing spray-dried powder thereof - Google Patents

Bacillus coagulans, high cell density fermentation method thereof, and method for preparing spray-dried powder thereof Download PDF

Info

Publication number
WO2017012570A1
WO2017012570A1 PCT/CN2016/090895 CN2016090895W WO2017012570A1 WO 2017012570 A1 WO2017012570 A1 WO 2017012570A1 CN 2016090895 W CN2016090895 W CN 2016090895W WO 2017012570 A1 WO2017012570 A1 WO 2017012570A1
Authority
WO
WIPO (PCT)
Prior art keywords
fermentation
shake flask
bacillus coagulans
culture
peptone
Prior art date
Application number
PCT/CN2016/090895
Other languages
French (fr)
Chinese (zh)
Inventor
张梁
Original Assignee
江南大学
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 江南大学 filed Critical 江南大学
Priority to AU2016297402A priority Critical patent/AU2016297402B2/en
Publication of WO2017012570A1 publication Critical patent/WO2017012570A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • 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
    • C12N1/205Bacterial isolates
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12RINDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/07Bacillus
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • 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

Definitions

  • the present invention relates to the field of microbial technology, and in particular to a Bacillus coagulans and a high-density fermentation method thereof and a prepared dry powder.
  • Microecological preparations are microbial agents prepared by a special process and contain microorganisms beneficial to the host.
  • Micro-developing agents have natural and non-toxic effects and promote the health of the host, and are increasingly used in human health and animal health.
  • Lactic acid bacteria and Bacillus microecological preparations are the two most widely used varieties in the feed industry.
  • the lactic acid bacteria mainly include lactic acid bacteria, bifidobacteria, etc.
  • the bacilli mainly include Bacillus subtilis, Bacillus licheniformis and the like.
  • Lactic acid fungi microecological preparations function by producing lactic acid, changing intestinal pH, and regulating the intestinal microenvironment. Such microecological preparations have poor resistance to stress and are prone to loss of activity during processing. Bacillus microecological preparations can produce spores, can withstand high temperature, stomach acid, choline and other adverse environments, and have strong resistance to stress, but they do not have the intestinal conditioning function of lactic acid bacteria.
  • Bacillus coagulans Gram-positive bacteria, a lactic acid-producing Bacillus
  • Bacillus coagulans is characterized by: 1. Producing lactic acid under the anaerobic environment of the intestine, forming an acidic environment, inhibiting the growth of pathogenic microorganisms, and beneficial to the health of the host; 2. It can exist in the state of spores, high temperature tolerance, gastric acid tolerance, choline resistance, environment Strong resistance to stress. It can be said that Bacillus coagulans has the advantages of both lactic acid bacteria and microbial preparations of Bacillus.
  • Bacillus coagulans Due to its good feeding and processing properties, Bacillus coagulans has been included in the list of feed additives and has become an important member of the feed microecological preparation industry.
  • ZL 201110428027.7 announced a process for solid state fermentation of Bacillus coagulans CICC No.20138, the cell amount 1.16x 10 1Q cfu / g, Bacillus rate 77.2 ⁇ 3 ⁇ 4.
  • the Applicant provides a Bacillus coagulans and a high-density fermentation method thereof, and a method for preparing a dry powder.
  • the invention is a new burst of Bacillus coagulans, which has the characteristics of high-density fermentation and high bacterial content, is beneficial to reducing product cost, contributing to product marketing, and has positive significance for promoting healthy breeding of livestock and poultry.
  • the Bacillus coagulcmi) provided by the present invention has been preserved in the China Center for Type Culture Collection, Culture Collection No. CCTCC M 2015273. This is achieved by the following steps:
  • strain numbered ZS-007 was finally obtained and identified as Bacillus coagula.
  • ZS-007 was deposited with the China Type Culture Collection on May 3, 2015 under the accession number CCTCC M 2015273.
  • Bacillus coagulans lactic acid production test Bacillus coagulans ZS-007 was inoculated into an acidogenicity test medium, and statically cultured at 37 ° C to carry out a lactic acid production test.
  • the acid-producing test medium used was: glucose 20 g/L, peptone 10 g/L, yeast powder 5 g/L, potassium dihydrogen phosphate 2 g/L, magnesium sulfate lg/L, manganese sulfate 0.5
  • the medium was adjusted to pH 7.0 with 10 ⁇ 3 ⁇ 4 NaOH and sterilized at 121 °C for 20 min.
  • lactic acid content in the fermentation broth was measured by HPLC, and the results are shown in FIG. It can be seen from Fig. 1 that the lactic acid content is about 10 g/L.
  • Bacillus coagulans strain is inoculated onto the nutrient agar slant medium, and cultured at 25-37 ° C for 24-48 hr; then the streak is transferred to the slant of the nutrient agar eggplant bottle, and cultured at 25-37 ° C 24- 48hr.
  • composition of the nutrient agar slant medium and the nutrient agar eggplant bottle are: peptone 10g / L, beef cream
  • the activated strain was inoculated into a shake flask and shake cultured for 18-30 hr.
  • Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L,
  • the volume of the 250 mL shake flask is 20 mL, and the volume of the 500 mL shake flask is 50 mL.
  • Seed tank medium composition peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4.
  • the seed tank has a volume of 10-1000L and a liquid volume of 50-80%.
  • the seed liquid is connected to the fermenter with an inoculum of 0.1%-10 ⁇ 3 ⁇ 4, and the fermentation medium is composed of: glucose 25 g/L, peptone 15 g/L, yeast powder 10 g/L, potassium dihydrogen phosphate lg /L, magnesium sulfate 0.5 g / L, initial pH 7.0.
  • the fermenter has a volume of l-50m 3 and a liquid loading of 50-80%.
  • the viable cell count and the number of spores of the final fermentation broth were measured by a plate coating method, and the spore rate was calculated.
  • the spore rate is the ratio of the number of spores to the number of viable cells.
  • the medium used was a nutrient agar medium: peptone 10 g/L, beef extract 3 g/L, sodium chloride 5 g/L, agar 15-20 g/L, pH 7.2-7.4.
  • the number of live bacteria in the final fermentation broth was measured and determined by gradient dilution; the number of spores was determined, and the final fermentation broth was heat-treated at 80 ° C for 10 min, and the mixture was diluted by a gradient.
  • the number of viable cells in the final fermentation broth was 1.5 ⁇ 10 1Q cfu/mL or more, the number of spores was 1.4 10 /!1 ⁇ or more, and the spore rate was 90.8% or more.
  • the wet bacterial sludge is collected, and the dry bacterial powder is obtained by a spray drying process.
  • Operating conditions are: inlet air temperature 210 °C, outlet air temperature 100 °C.
  • the number of viable bacteria in dry powder is 8.0x10 "cfu/g or more.
  • the obtained dry powder can be mixed with a filler such as starch, glucose, and other standards-compliant carriers to obtain a Bacillus coagulans microecological preparation.
  • a filler such as starch, glucose, and other standards-compliant carriers to obtain a Bacillus coagulans microecological preparation.
  • the present invention employs a liquid fermentation process in which the number of viable bacteria in the fermentation broth is 1.52 ⁇ 10 i. Above cfu/mL, the number of spores was 1.38x10 W cfu/mL or more, and the spore rate was 90.8% or more. In the dry powder obtained by spray drying, the number of viable cells was 8.0 x 10 11 cfu/g or more.
  • the dry powder can be mixed with a filler such as starch or glucose to obtain a coagulating microbial preparation.
  • the production process of the invention is simple and stable, and the number of viable bacteria in the fermentation liquid is high, which can directly reduce the application cost and is beneficial to product promotion. This has implications for the widespread use of Bacillus coagulans microecological preparations.
  • 1 is a HPLC method for detecting lactic acid content in a fermentation broth of Bacillus coagulans according to the present invention.
  • ZS-007 was deposited with the China Type Culture Collection on May 3, 2015 under the accession number CCTCC M 2015273.
  • Example 1 The strain obtained in Example 1 was inoculated on a nutrient agar slant medium, cultured at 30 ° C for 24 hours, and then streaked to the slant of the nutrient agar eggplant bottle, and cultured at 30 ° C for 24 hr.
  • the composition of nutrient agar slant medium and nutrient agar eggplant bottle are: peptone 10g/L, beef extract 3g/L, sodium chloride 5g/L, agar 15-20g/L, pH 7.2-7.4.
  • Shake flask culture The activated strain was inoculated into a shake flask and shake cultured for 20 hr.
  • Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4, shake flask volume 50mL / 500mL triangle bottle.
  • Culture conditions shake flask speed 200r/min, temperature 30. C.
  • Fermentor Fermentation 20 bottles of flask liquid were collected as seeds for access to the lm 3 fermentor.
  • the lm 3 fermenter has a liquid volume of 65%.
  • Medium composition glucose 25 g/L, peptone 15 g/L, yeast powder 10
  • the cultured seeds are connected to the fermenter for fermentation. Culture conditions: stirring speed 200 r / min, aeration rate 0.8 wm, temperature 30 ° C, culture day 40-44 hr.
  • Shake flask culture The activated strain was inoculated into a shake flask and shake cultured for 20 hr.
  • Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4, shake flask volume is 20mL / 250mL triangle bottle.
  • Culture conditions shake flask speed 200r / min, temperature 30 ° C.
  • Seed tank expansion Collect 10 bottles of 250 mL shake flask seed solution for seed tank inoculation.
  • Seed tank medium composition peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4.
  • the seed tank has a volume of 30L and a liquid volume of 80 ⁇ 3 ⁇ 4.
  • Culture conditions stirring speed 200 r / min, aeration 0.8 vvm, temperature 30 ° C, incubation time 20 hr.
  • Fermentor Fermentation The liquid volume of the 3 m 3 fermenter was 70%. Medium composition: glucose 25 g / L, peptone 15 g / L, yeast powder 10 g / L, potassium dihydrogen phosphate lg / L, magnesium sulfate 0.5 g / L, initial pH 7.0. The cultured seeds are connected to a fermentor for fermentation. Culture conditions: stirring speed 150 r / min, aeration of 0.7 V vm, temperature 35 ° C, cultured for 36-42 hr.
  • the number of viable cells was 1.79 ⁇ 10 1 () cfu/g
  • the number of spores was 1.72 ⁇ 10 1 () cfu/g
  • the spore rate was 96.1 ⁇ 3 ⁇ 4.
  • Shake flask culture The activated strain was inoculated into a shake flask and shake cultured for 20 hr.
  • Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4, shake flask volume 50mL / 500mL triangle bottle.
  • Culture conditions shake flask speed 200r/min, temperature 30. C.
  • Seed tank expansion 20 bottles of 500 mL shake flask seed solution were collected for seed tank inoculation.
  • Seed tank medium composition peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4.
  • the seed tank has a volume of 500L and a liquid volume of 75%.
  • Culture conditions stirring speed 200 r / min, aeration rate 0.8 vvm, temperature 30 ° C, culture time 20 hr.
  • Fermentor Fermentation The amount of liquid in the 30 m 3 fermenter is 70%.
  • Medium composition glucose 25 g / L, peptone 15 g / L, yeast powder 10 g / L, potassium dihydrogen phosphate lg / L, magnesium sulfate 0.5 g / L, initial pH 7.0.
  • the cultured seeds are connected to a fermentor for fermentation.
  • Culture conditions stirring speed 100 r / min, aeration rate 0.6 v V m, temperature 35 ° C, cultured for 40-45 hr.
  • the viable cell count was 1.99 ⁇ 10 1 ( cfu/g
  • the spore number was 1.92 ⁇ 10 1 ( cfu/g
  • the spore rate was 96.5 ⁇ 3 ⁇ 4.
  • the wet bacterial sludge is collected by centrifugation, and a dry bacterial powder is obtained by a spray drying process. Operating conditions are: inlet air temperature 210 °C, outlet air temperature 100 °C. The number of viable bacteria in dry powder is 8.32x10 "cfu/ga [0067]
  • Example 4 The fermentation broth of Example 4 was used to obtain a fermentation broth of Bacillus coagulans, and the wet bacterial sludge was collected by centrifugation, and a dry powder was obtained by a spray drying process. Operating conditions are: inlet air temperature 220 °C, outlet air temperature 100 °C. Number of viable bacteria in dry powder 6.54x10 "cfu/ga

Abstract

Provided is a Bacillus coagulans strain (serial number: ZS-007) deposited in the China Center for Type Culture Collection (CCTCC) and having a deposition number of CCTCC M2015273. Also provided are a fermentation method of the Bacillus coagulans (serial number: ZS-007), and method for preparing a spray-dried powder of the Bacillus coagulans via the fermentation method.

Description

说明书  Instruction manual
发明名称:一种凝结芽孢杆菌及其高密度发酵方法以及干菌粉制备 方法  Title: A Bacillus coagulans and a high-density fermentation method thereof, and a method for preparing dry powder
技术领域  Technical field
[0001] 本发明涉及微生物技术领域, 尤其是涉及一种凝结芽孢杆菌及其高密度发酵方 法以及制备得到的干菌粉。  [0001] The present invention relates to the field of microbial technology, and in particular to a Bacillus coagulans and a high-density fermentation method thereof and a prepared dry powder.
背景技术  Background technique
[0002] 微生态制剂是经特殊工艺制成的微生物菌剂, 含有对宿主有益的微生物。 微生 态制剂具有天然无毒、 促进宿主健康的作用, 在人体保健、 动物健康领域应用 日益广泛。  [0002] Microecological preparations are microbial agents prepared by a special process and contain microorganisms beneficial to the host. Micro-developing agents have natural and non-toxic effects and promote the health of the host, and are increasingly used in human health and animal health.
[0003] 乳酸菌类和芽孢杆菌类微生态制剂是饲料工业使用最为广泛的两大品种。 乳酸 菌类主要包括乳酸菌、 双歧杆菌等, 芽孢杆菌类主要包括枯草芽孢杆菌、 地衣 芽孢杆菌等。  [0003] Lactic acid bacteria and Bacillus microecological preparations are the two most widely used varieties in the feed industry. The lactic acid bacteria mainly include lactic acid bacteria, bifidobacteria, etc., and the bacilli mainly include Bacillus subtilis, Bacillus licheniformis and the like.
[0004] 乳酸菌类微生态制剂通过产乳酸、 改变肠道 pH、 调理肠道微环境发挥作用。 此 类微生态制剂抗逆性差, 在加工过程中易失去活性。 芽孢杆菌类微生态制剂能 产生芽孢, 可耐受高温、 胃酸、 胆碱等不良环境, 抗逆性强, 但其不具备乳酸 菌类的肠道调理功能。  [0004] Lactic acid fungi microecological preparations function by producing lactic acid, changing intestinal pH, and regulating the intestinal microenvironment. Such microecological preparations have poor resistance to stress and are prone to loss of activity during processing. Bacillus microecological preparations can produce spores, can withstand high temperature, stomach acid, choline and other adverse environments, and have strong resistance to stress, but they do not have the intestinal conditioning function of lactic acid bacteria.
[0005] 凝结芽孢杆菌 (Bacillus coagulans) , 革兰阳性菌, 是一种产乳酸的芽孢杆菌 [0005] Bacillus coagulans, Gram-positive bacteria, a lactic acid-producing Bacillus
。 凝结芽孢杆菌特点在于: 1, 肠道厌氧环境下产乳酸, 形成酸性环境, 抑制病 原微生物生长, 有益于宿主健康; 2, 能以芽孢状态存在, 耐高温、 耐胃酸、 耐 胆碱、 环境抗逆性强。 可以说, 凝结芽孢杆菌兼具乳酸菌类和芽孢杆菌类微生 态制剂的优点。 . Bacillus coagulans is characterized by: 1. Producing lactic acid under the anaerobic environment of the intestine, forming an acidic environment, inhibiting the growth of pathogenic microorganisms, and beneficial to the health of the host; 2. It can exist in the state of spores, high temperature tolerance, gastric acid tolerance, choline resistance, environment Strong resistance to stress. It can be said that Bacillus coagulans has the advantages of both lactic acid bacteria and microbial preparations of Bacillus.
[0006] 由于良好的饲喂效果和加工性能, 凝结芽孢杆菌已列入饲料添加剂名录, 成为 饲料微生态制剂行业的重要成员。  [0006] Due to its good feeding and processing properties, Bacillus coagulans has been included in the list of feed additives and has become an important member of the feed microecological preparation industry.
[0007] 人们对凝结芽孢杆菌的关注日益增多, 幵展了大量研究工作。 ZL200710122111 .X公布了一种凝结芽孢杆菌饲料添加剂的制备, 发酵液活菌数最高 5.0x10 9 cfu/mL。 ZL 200810235512.0公布了凝结芽胞杆菌 CGMCC No.2602的液态发酵工 艺。 IT发酵罐中, 发酵液总菌数 6.0x 10 9cfu/mL、 芽孢数 5.8x10 9 [0007] There has been an increasing interest in Bacillus coagulans, and a great deal of research has been done. ZL200710122111 .X published a preparation of a Bacillus coagulans feed additive with a maximum viable count of 5.0x10 9 cfu/mL. ZL 200810235512.0 announced the liquid fermenter of Bacillus coagulans CGMCC No. 2602 Art. In the IT fermenter, the total number of bacteria in the fermentation broth is 6.0x 10 9 cfu/mL, and the number of spores is 5.8x10 9
cfu/mL、 芽孢率 96.7<¾。 ZL 201110428027.7公布了一种凝结芽孢杆菌 CICC No.20138的固态发酵工艺, 菌体量 1.16x 10 1Qcfu/g、 芽孢率 77.2<¾。 ZL Cfu/mL, spore rate 96.7 <3⁄4. ZL 201110428027.7 announced a process for solid state fermentation of Bacillus coagulans CICC No.20138, the cell amount 1.16x 10 1Q cfu / g, Bacillus rate 77.2 <¾. ZL
201210464404.7公布了凝结芽胞杆菌 CGMCC No.6681的反馈补料培养工艺, 发 酵液活菌数最高 5.8x10 fu/mL。  201210464404.7 announced the feedback feeding culture process of Bacillus coagulans CGMCC No.6681, the highest number of live bacteria in the fermentation broth was 5.8x10 fu/mL.
[0008] 尽管业界幵展了大量研究工作, 但市场上凝结芽孢杆菌的售价依然居高不下, 产品推广有一定难度。 究其原因, 还是凝结芽孢杆菌产业化发酵水平低、 加工 过程菌体损失高、 成品菌体含量低。 这些不利因素直接造成产品价格高, 影响 凝结芽孢杆菌的普及应用。 [0008] Despite the extensive research work in the industry, the price of Bacillus coagulans in the market is still high, and product promotion is difficult. The reason is that the industrial fermentation level of Bacillus coagulans is low, the loss of bacteria in the processing process is high, and the content of the finished cells is low. These unfavorable factors directly lead to high product prices, affecting the widespread use of Bacillus coagulans.
技术问题  technical problem
[0009] 针对现有技术存在的上述问题, 本申请人提供了一种凝结芽孢杆菌及其高密度 发酵方法以及干菌粉制备方法。 本发明是新幵发的凝结芽孢杆菌, 具有高密度 发酵和高菌体含量的特点, 有利于降低产品成本, 有助于产品市场推广, 对于 促进畜禽健康养殖具有积极意义。  In view of the above problems in the prior art, the Applicant provides a Bacillus coagulans and a high-density fermentation method thereof, and a method for preparing a dry powder. The invention is a new burst of Bacillus coagulans, which has the characteristics of high-density fermentation and high bacterial content, is beneficial to reducing product cost, contributing to product marketing, and has positive significance for promoting healthy breeding of livestock and poultry.
问题的解决方案  Problem solution
技术解决方案  Technical solution
[0010] 本发明的技术方案如下: [0010] The technical solution of the present invention is as follows:
[0011] 本发明提供的凝结芽孢杆菌 Bacillus coagulcmi) 已保存于中国典型培养物保 藏中心, 菌种保藏号 CCTCC M 2015273。 具体是通过以下步骤来实现的:  [0011] The Bacillus coagulcmi) provided by the present invention has been preserved in the China Center for Type Culture Collection, Culture Collection No. CCTCC M 2015273. This is achieved by the following steps:
[0012] 1、 凝结芽孢杆菌的筛选 [0012] 1. Screening of Bacillus coagulans
[0013] 从江苏无锡马山某奶牛养殖场附近的土壤样品称取 2g, 加入 98ml无菌生理盐水 , 80°C热处理 lOmin后, 在 37°C摇床上 120 rpm条件下振荡 20min, 吸取上清液 lml 加入 LB培养基中稀释涂布进行菌株分离。 通过对菌株进行形态学观察、 生理生 化实验、 16S rDNA分析等手段有效而准确的确定菌种的属种。  [0013] Weigh 2g from the soil sample near a dairy farm in Mashan, Wuxi, Jiangsu, add 98ml of sterile physiological saline, heat treatment at 80 °C for 10 minutes, shake at 120 rpm on a 37 °C shaker for 20 min, absorb the supernatant The liquid was added to LB medium and diluted and coated for strain isolation. The species of the strain were effectively and accurately determined by means of morphological observation, physiological bioassay, and 16S rDNA analysis.
[0014] 最终得到编号为 ZS-007的菌种, 鉴定为凝结芽孢杆菌 Bacillus coagula ) 。  [0014] The strain numbered ZS-007 was finally obtained and identified as Bacillus coagula.
[0015] ZS-007于 2015年 5月 3日保藏于中国典型培养物保藏中心, 保藏编号为 CCTCC M 2015273。  [0015] ZS-007 was deposited with the China Type Culture Collection on May 3, 2015 under the accession number CCTCC M 2015273.
[0016] 2、 凝结芽孢杆菌的产乳酸能力测试 [0017] 将凝结芽孢杆菌 ZS-007接种于产酸能力测试培养基中, 并在 37°C下静置培养进 行产乳酸能力测试。 所用产酸能力测试培养基组成为: 葡萄糖 20 g/L, 蛋白胨 10 g/L, 酵母粉 5 g/L, 磷酸二氢钾 2 g/L, 硫酸镁 l g/L, 硫酸锰 0.5 [0016] 2, Bacillus coagulans lactic acid production test [0017] Bacillus coagulans ZS-007 was inoculated into an acidogenicity test medium, and statically cultured at 37 ° C to carry out a lactic acid production test. The acid-producing test medium used was: glucose 20 g/L, peptone 10 g/L, yeast powder 5 g/L, potassium dihydrogen phosphate 2 g/L, magnesium sulfate lg/L, manganese sulfate 0.5
g/L。 培养基用 10<¾NaOH调节 pH7.0后, 121 °C灭菌 20 min。  g/L. The medium was adjusted to pH 7.0 with 10<3⁄4 NaOH and sterilized at 121 °C for 20 min.
[0018] 利用 HPLC检测发酵液中的乳酸含量, 结果见图 1。 从图 1中可以看到乳酸含量 在 10g/L左右。  [0018] The lactic acid content in the fermentation broth was measured by HPLC, and the results are shown in FIG. It can be seen from Fig. 1 that the lactic acid content is about 10 g/L.
[0019] 3、 凝结芽孢杆菌高密度发酵  [0019] 3, Bacillus coagulum high-density fermentation
[0020] (1) 菌种活化  (1) Activation of strains
[0021] 将凝结芽孢杆菌菌种接种至营养琼脂斜面培养基上, 25-37°C下培养 24-48hr; 然后划线转接于营养琼脂茄子瓶斜面, 25-37°C下培养 24-48hr。  [0021] The Bacillus coagulans strain is inoculated onto the nutrient agar slant medium, and cultured at 25-37 ° C for 24-48 hr; then the streak is transferred to the slant of the nutrient agar eggplant bottle, and cultured at 25-37 ° C 24- 48hr.
[0022] 营养琼脂斜面培养基及营养琼脂茄子瓶的组成均为: 蛋白胨 10g/L, 牛肉膏[0022] The composition of the nutrient agar slant medium and the nutrient agar eggplant bottle are: peptone 10g / L, beef cream
3g/L, 氯化钠 5g/L, 琼脂 15-20g/L, pH7.2-7.4。 3 g/L, sodium chloride 5 g/L, agar 15-20 g/L, pH 7.2-7.4.
[0023] (2) 摇瓶培养 [0023] (2) Shake flask culture
[0024] 将活化好的菌种接种至摇瓶中, 振荡培养 18-30hr。  [0024] The activated strain was inoculated into a shake flask and shake cultured for 18-30 hr.
[0025] 摇瓶培养基配方: 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L,  [0025] Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L,
pH7.2-7.4。 250mL摇瓶装液量为 20mL, 500mL摇瓶装液量为 50mL。  pH 7.2-7.4. The volume of the 250 mL shake flask is 20 mL, and the volume of the 500 mL shake flask is 50 mL.
[0026] 培养条件: 摇瓶转速 200r/min, 温度 25-37°C。 [0026] Culture conditions: shake flask speed 200 r/min, temperature 25-37 °C.
[0027] (3) 种子罐扩培 [0027] (3) Seed tank expansion
[0028] 扩培菌种以用于后期发酵。 种子罐培养基组成: 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L, pH7.2-7.4。 种子罐体积 10-1000L, 装液量 50-80%。  [0028] Expanded strains for later fermentation. Seed tank medium composition: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4. The seed tank has a volume of 10-1000L and a liquid volume of 50-80%.
[0029] 培养条件: 搅拌转速 180-250r/min, 通气量 0.5-1.0vvm, 温度 25-37°C, 培养吋 间 18-30hr。  [0029] Culture conditions: stirring speed 180-250r/min, aeration amount 0.5-1.0vvm, temperature 25-37 ° C, culture time between 18-30hr.
[0030] (4) 发酵罐发酵  [0030] (4) Fermentor Fermentation
[0031] 以 0.1%-10<¾的接种量将种子液接入发酵罐, 发酵培养基组成: 葡萄糖 25 g/L, 蛋白胨 15 g/L, 酵母粉 10 g/L, 磷酸二氢钾 l g/L, 硫酸镁 0.5 g/L, 初始 pH7.0。 发 酵罐体积 l-50m 3, 装液量 50-80%。 [0031] The seed liquid is connected to the fermenter with an inoculum of 0.1%-10<3⁄4, and the fermentation medium is composed of: glucose 25 g/L, peptone 15 g/L, yeast powder 10 g/L, potassium dihydrogen phosphate lg /L, magnesium sulfate 0.5 g / L, initial pH 7.0. The fermenter has a volume of l-50m 3 and a liquid loading of 50-80%.
[0032] 培养条件: 搅拌转速 100-200r/min, 通气量 0.5-0.8vvm, 温度 25-37°C, 培养吋 间 16-48hr。 [0033] 取发酵液镜检吋, 当 90%以上的菌体都形成芽孢吋, 即到发酵终点, 得到最终 发酵液。 [0032] Culture conditions: agitation speed of 100-200 r / min, aeration of 0.5-0.8 vvm, temperature of 25-37 ° C, cultured for 16-48 hr. [0033] Taking the fermentation liquid microscopic examination, when more than 90% of the cells form spores, that is, to the end of the fermentation, the final fermentation liquid is obtained.
[0034] 采用平板涂布法测定最终发酵液活菌数和芽孢数, 并计算芽孢率。 其中, 芽孢 率为芽孢数与活菌数的比值。 所用培养基为营养琼脂培养基: 蛋白胨 10g/L, 牛 肉膏 3g/L, 氯化钠 5g/L, 琼脂 15-20g/L, pH7.2-7.4。 测定最终发酵液活菌数吋 , 梯度稀释后测定; 测定芽孢数吋, 取最终发酵液于 80°C热处理 10min, 梯度稀 释后测定。 最终发酵液中活菌数 1.5x10 1Qcfu/mL以上、 芽孢数1.4 10 /!1^以 上、 芽孢率 90.8%以上。 [0034] The viable cell count and the number of spores of the final fermentation broth were measured by a plate coating method, and the spore rate was calculated. Among them, the spore rate is the ratio of the number of spores to the number of viable cells. The medium used was a nutrient agar medium: peptone 10 g/L, beef extract 3 g/L, sodium chloride 5 g/L, agar 15-20 g/L, pH 7.2-7.4. The number of live bacteria in the final fermentation broth was measured and determined by gradient dilution; the number of spores was determined, and the final fermentation broth was heat-treated at 80 ° C for 10 min, and the mixture was diluted by a gradient. The number of viable cells in the final fermentation broth was 1.5×10 1Q cfu/mL or more, the number of spores was 1.4 10 /!1^ or more, and the spore rate was 90.8% or more.
[0035] 4、 干菌粉制备  [0035] 4, dry powder preparation
[0036] 最终发酵液离心后收集湿菌泥, 采用喷雾干燥工艺得到干菌粉。 操作条件为: 进风温度 210 °C, 出风温度 100 °C。 干菌粉中活菌数 8.0x10 "cfu/g以上。  [0036] After the final fermentation broth is centrifuged, the wet bacterial sludge is collected, and the dry bacterial powder is obtained by a spray drying process. Operating conditions are: inlet air temperature 210 °C, outlet air temperature 100 °C. The number of viable bacteria in dry powder is 8.0x10 "cfu/g or more.
[0037] 所得干菌粉可与淀粉、 葡萄糖、 以及其它符合标准的载体等填充剂混合后得到 凝结芽孢杆菌微生态制剂。 [0037] The obtained dry powder can be mixed with a filler such as starch, glucose, and other standards-compliant carriers to obtain a Bacillus coagulans microecological preparation.
发明的有益效果  Advantageous effects of the invention
有益效果  Beneficial effect
[0038] 本发明有益的技术效果在于: [0038] The beneficial technical effects of the present invention are:
[0039] 本发明采用液体发酵工艺, 发酵液中凝结芽孢杆菌活菌数 1.52x10 i。cfu/mL以 上、 芽孢数 1.38x10 W cfu/mL以上、 芽孢率 90.8%以上。 喷雾干燥获得的干菌粉中 , 活菌数 8.0x10 11 cfu/g以上。 干菌粉可与淀粉、 葡萄糖等填充剂混合后得到凝结 芽孢杆菌微生态制剂。  [0039] The present invention employs a liquid fermentation process in which the number of viable bacteria in the fermentation broth is 1.52×10 i. Above cfu/mL, the number of spores was 1.38x10 W cfu/mL or more, and the spore rate was 90.8% or more. In the dry powder obtained by spray drying, the number of viable cells was 8.0 x 10 11 cfu/g or more. The dry powder can be mixed with a filler such as starch or glucose to obtain a coagulating microbial preparation.
[0040] 本发明生产工艺简单稳定, 发酵液中活菌数高, 可直接减少应用成本, 有利于 产品推广。 这对于推动凝结芽孢杆菌微生态制剂的广泛应用具有意义。  [0040] The production process of the invention is simple and stable, and the number of viable bacteria in the fermentation liquid is high, which can directly reduce the application cost and is beneficial to product promotion. This has implications for the widespread use of Bacillus coagulans microecological preparations.
对附图的简要说明  Brief description of the drawing
附图说明  DRAWINGS
[0041] 图 1为本发明凝结芽孢杆菌的 HPLC检测发酵液中的乳酸含量。  1 is a HPLC method for detecting lactic acid content in a fermentation broth of Bacillus coagulans according to the present invention.
本发明的实施方式 [0042] 实施例 1 : 凝结芽孢杆菌的筛选 Embodiments of the invention Example 1: Screening of Bacillus coagulans
[0043] 从江苏无锡马山某奶牛养殖场附近的土壤样品称取 2g, 加入 98ml无菌生理盐水 , 80°C热处理 lOmin后, 在 37°C摇床上 120 rpm条件下振荡 20min, 吸取上清液 1 ml加入 LB培养基中稀释涂布进行菌株分离。 通过对菌株进行形态学观察、 生理 生化实验、 16S rDNA分析等手段有效而准确的确定菌种的属种。  [0043] Weigh 2g from the soil sample near a dairy farm in Mashan, Wuxi, Jiangsu Province, add 98ml of sterile physiological saline, heat treatment at 80 °C for 10 minutes, shake at 120 rpm on a 37 °C shaker for 20 min, absorb the supernatant 1 ml of the solution was added to LB medium and diluted and coated for strain isolation. The species of the strain were effectively and accurately determined by means of morphological observation, physiological and biochemical experiments, and 16S rDNA analysis.
[0044] 最终得到编号为 ZS-007的菌种, 鉴定为凝结芽孢杆菌 Bacillus coagula ) 。 [0044] The strain numbered ZS-007 was finally obtained and identified as Bacillus coagula.
[0045] ZS-007于 2015年 5月 3日保藏于中国典型培养物保藏中心, 保藏编号为 CCTCC M 2015273。 [0045] ZS-007 was deposited with the China Type Culture Collection on May 3, 2015 under the accession number CCTCC M 2015273.
[0046]  [0046]
[0047] 实施例 2: lm 3发酵罐制备 Example 2: Preparation of lm 3 fermentor
[0048] 菌种活化: 将实施例 1得到的菌种接种至营养琼脂斜面培养基上, 30°C下培养 2 4hr后划线转接于营养琼脂茄子瓶斜面, 30°C下培养 24hr。 营养琼脂斜面培养基 及营养琼脂茄子瓶的组成均为: 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L, 琼脂 15-20g/L, pH7.2-7.4。  [0048] Activation of the strain: The strain obtained in Example 1 was inoculated on a nutrient agar slant medium, cultured at 30 ° C for 24 hours, and then streaked to the slant of the nutrient agar eggplant bottle, and cultured at 30 ° C for 24 hr. The composition of nutrient agar slant medium and nutrient agar eggplant bottle are: peptone 10g/L, beef extract 3g/L, sodium chloride 5g/L, agar 15-20g/L, pH 7.2-7.4.
[0049] 摇瓶培养: 将活化好的菌种接种至摇瓶中, 振荡培养 20hr。 摇瓶培养基配方: 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L, pH7.2-7.4 , 摇瓶装液量 50mL/500mL 三角瓶。 培养条件: 摇瓶转速 200r/min, 温度 30。C。  [0049] Shake flask culture: The activated strain was inoculated into a shake flask and shake cultured for 20 hr. Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4, shake flask volume 50mL / 500mL triangle bottle. Culture conditions: shake flask speed 200r/min, temperature 30. C.
[0050] 发酵罐发酵: 收集 20瓶三角瓶液体作为种子接入 lm 3发酵罐。 lm 3发酵罐装液 量 65%。 培养基组成: 葡萄糖 25 g/L, 蛋白胨 15 g/L, 酵母粉 10  [0050] Fermentor Fermentation: 20 bottles of flask liquid were collected as seeds for access to the lm 3 fermentor. The lm 3 fermenter has a liquid volume of 65%. Medium composition: glucose 25 g/L, peptone 15 g/L, yeast powder 10
g/L, 磷酸二氢钾 l g/L, 硫酸镁 0.5 g/L, 初始 pH7.0。 将培养好的种子接入发酵罐 进行发酵。 培养条件: 搅拌转速 200r/min, 通气量 0.8wm, 温度 30°C, 培养吋间 40-44hr。  g/L, potassium dihydrogen phosphate l g/L, magnesium sulfate 0.5 g/L, initial pH 7.0. The cultured seeds are connected to the fermenter for fermentation. Culture conditions: stirring speed 200 r / min, aeration rate 0.8 wm, temperature 30 ° C, culture day 40-44 hr.
[0051] 发酵液中, 活菌数 1.52x 10 1Qcfu/g, 芽孢数 1.38x10 1Qcfu/g, 芽孢率 90.8<¾。 [0051] broth, viable cell count 1.52x 10 1Q cfu / g, the number of spores 1.38x10 1Q cfu / g, Bacillus rate 90.8 <¾.
[0052] [0052]
[0053] 实施例 3 : 3m 3发酵罐制备 Example 3: Preparation of 3m 3 Fermentor
[0054] 菌种活化同实施例 2。 [0054] The species activation was the same as in Example 2.
[0055] 摇瓶培养: 将活化好的菌种接种至摇瓶中, 振荡培养 20hr。 摇瓶培养基配方: 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L, pH7.2-7.4, 摇瓶装液量为 20mL/250mL三角瓶。 培养条件: 摇瓶转速 200r/ min, 温度 30°C。 [0055] Shake flask culture: The activated strain was inoculated into a shake flask and shake cultured for 20 hr. Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4, shake flask volume is 20mL / 250mL triangle bottle. Culture conditions: shake flask speed 200r / min, temperature 30 ° C.
[0056] 种子罐扩培: 收集 10瓶 250mL摇瓶种子液用于种子罐接种。 种子罐培养基组成 : 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L, pH7.2-7.4。 种子罐体积 30L, 装液 量 80<¾。 培养条件: 搅拌转速 200r/min, 通气量 0.8vvm, 温度 30°C, 培养吋间 20 hr。  [0056] Seed tank expansion: Collect 10 bottles of 250 mL shake flask seed solution for seed tank inoculation. Seed tank medium composition: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4. The seed tank has a volume of 30L and a liquid volume of 80<3⁄4. Culture conditions: stirring speed 200 r / min, aeration 0.8 vvm, temperature 30 ° C, incubation time 20 hr.
[0057] 发酵罐发酵: 3m 3发酵罐装液量 70%。 培养基组成: 葡萄糖 25 g/L, 蛋白胨 15 g/L, 酵母粉 10 g/L, 磷酸二氢钾 l g/L, 硫酸镁 0.5 g/L, 初始 pH7.0。 将培养好的 种子接入发酵罐进行发酵。 培养条件: 搅拌转速 150r/min, 通气量 0.7Vvm, 温度 35°C, 培养吋间 36-42hr。 [0057] Fermentor Fermentation: The liquid volume of the 3 m 3 fermenter was 70%. Medium composition: glucose 25 g / L, peptone 15 g / L, yeast powder 10 g / L, potassium dihydrogen phosphate lg / L, magnesium sulfate 0.5 g / L, initial pH 7.0. The cultured seeds are connected to a fermentor for fermentation. Culture conditions: stirring speed 150 r / min, aeration of 0.7 V vm, temperature 35 ° C, cultured for 36-42 hr.
[0058] 发酵液中, 活菌数 1.79x10 1()cfu/g, 芽孢数 1.72x10 1()cfu/g, 芽孢率 96.1<¾。 [0058] In the fermentation broth, the number of viable cells was 1.79× 10 1 () cfu/g, the number of spores was 1.72× 10 1 () cfu/g, and the spore rate was 96.1<3⁄4.
[0059]  [0059]
[0060] 实施例 4: 30m 3发酵罐和干菌粉制备  Example 4: Preparation of 30m 3 fermentor and dry powder
[0061] 菌种活化同实施例 2 [0061] Strain activation is the same as in Example 2
[0062] 摇瓶培养: 将活化好的菌种接种至摇瓶中, 振荡培养 20hr。 摇瓶培养基配方: 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L, pH7.2-7.4, 摇瓶装液量 50mL/500mL 三角瓶。 培养条件: 摇瓶转速 200r/min, 温度 30。C。  [0062] Shake flask culture: The activated strain was inoculated into a shake flask and shake cultured for 20 hr. Shake flask medium formula: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4, shake flask volume 50mL / 500mL triangle bottle. Culture conditions: shake flask speed 200r/min, temperature 30. C.
[0063] 种子罐扩培: 收集 20瓶 500mL摇瓶种子液用于种子罐接种。 种子罐培养基组成 : 蛋白胨 10g/L, 牛肉膏 3g/L, 氯化钠 5g/L, pH7.2-7.4。 种子罐体积 500L, 装 液量 75%。 培养条件: 搅拌转速 200r/min, 通气量 0.8vvm, 温度 30°C, 培养吋间 20hr。  [0063] Seed tank expansion: 20 bottles of 500 mL shake flask seed solution were collected for seed tank inoculation. Seed tank medium composition: peptone 10g / L, beef extract 3g / L, sodium chloride 5g / L, pH 7.2-7.4. The seed tank has a volume of 500L and a liquid volume of 75%. Culture conditions: stirring speed 200 r / min, aeration rate 0.8 vvm, temperature 30 ° C, culture time 20 hr.
[0064] 发酵罐发酵: 30m 3发酵罐装液量 70%。 培养基组成: 葡萄糖 25 g/L, 蛋白胨 15 g/L, 酵母粉 10 g/L, 磷酸二氢钾 l g/L, 硫酸镁 0.5 g/L, 初始 pH7.0。 将培养好的 种子接入发酵罐进行发酵。 培养条件: 搅拌转速 100r/min, 通气量 0.6vVm, 温度 35°C, 培养吋间 40-45hr。 [0064] Fermentor Fermentation: The amount of liquid in the 30 m 3 fermenter is 70%. Medium composition: glucose 25 g / L, peptone 15 g / L, yeast powder 10 g / L, potassium dihydrogen phosphate lg / L, magnesium sulfate 0.5 g / L, initial pH 7.0. The cultured seeds are connected to a fermentor for fermentation. Culture conditions: stirring speed 100 r / min, aeration rate 0.6 v V m, temperature 35 ° C, cultured for 40-45 hr.
[0065] 发酵液中, 活菌数 1.99x10 1(cfu/g, 芽孢数 1.92x10 1(cfu/g, 芽孢率 96.5<¾。 [0065] In the fermentation broth, the viable cell count was 1.99× 10 1 ( cfu/g, the spore number was 1.92× 10 1 ( cfu/g, and the spore rate was 96.5<3⁄4.
[0066] 离心收集湿菌泥, 采用喷雾干燥工艺得到干菌粉。 操作条件为: 进风温度 210 °C, 出风温度 100 °C。 干菌粉中活菌数 8.32x10 "cfu/ga [0067] [0066] The wet bacterial sludge is collected by centrifugation, and a dry bacterial powder is obtained by a spray drying process. Operating conditions are: inlet air temperature 210 °C, outlet air temperature 100 °C. The number of viable bacteria in dry powder is 8.32x10 "cfu/ga [0067]
[0068] 实施例 5: 干菌粉制备  Example 5: Preparation of dried powder
[0069] 采用实施例 4中的发酵方法获得凝结芽胞杆菌发酵液, 离心收集湿菌泥, 采用 喷雾干燥工艺得到干菌粉。 操作条件为: 进风温度 220 °C, 出风温度 100 °C。 干 菌粉中活菌数 6.54x10 "cfu/ga  The fermentation broth of Example 4 was used to obtain a fermentation broth of Bacillus coagulans, and the wet bacterial sludge was collected by centrifugation, and a dry powder was obtained by a spray drying process. Operating conditions are: inlet air temperature 220 °C, outlet air temperature 100 °C. Number of viable bacteria in dry powder 6.54x10 "cfu/ga
[0070]  [0070]
[0071] 对于本领域技术人员来说, 可以根据上述说明加以改进或变换, 这些改进或变 换都属于本发明所附权利要求的保护范围。 [0071] It will be apparent to those skilled in the art that the present invention may be modified or altered in light of the above description.
打印件 (原件为电子形式) Print (original is in electronic form)
0-1 PCT/RO/134表 (SAFE)有关保藏的微生物  0-1 PCT/RO/134 Table (SAFE) on preserved microorganisms
或其他生物材料的说明 (PCT细则笫 13条  Or description of other biological materials (PCT Article 笫 13
之二)  of two)
0-1-1 软件版本 CEPCT  0-1-1 Software Version CEPCT
版本 1.01.00 MT/FOP 20140331/0.20.5.21  Version 1.01.00 MT/FOP 20140331/0.20.5.21
0-2 国际申请号 PCT/CN2016/090895  0-2 International Application No. PCT/CN2016/090895
0-3 申请人或代理人的档案号 HY0082  0-3 File number of the applicant or agent HY0082
1 下面的说明与本申请说明书中此处提到的 1 The following instructions are mentioned here with the instructions in this application.
保藏的微生物或其他生物材料相关:  Preserved microorganisms or other biological materials related:
1-1 页码 0015  1-1 Page 0015
1-2 行号: 1-2  1-2 line number: 1-2
1-3 保藏事项  1-3 Deposits
1-3-1 保藏单位名称 中国典型培养物保藏中心  1-3-1 Depository Name China National Culture Collection
1-3-2 保藏单位地址 中国湖北省武汉市武汉大学,邮政编码: 430072, Hubei  1-3-2 Depository Address Wuhan University, Wuhan, Hubei Province, China, 430072, Hubei
(CN)。  (CN).
1-3-3 保藏日期 2015年 5月 03日(03.05.2015)  1-3-3 Deposit Date May 03, 2015 (03.05.2015)
1-3-4 保藏号 CCTCC M2015273  1-3-4 Deposit No. CCTCC M2015273
1-4 补充说明  1-4 Supplementary explanation
1-5 本说明是对下列指定国 所有指定国  1-5 This note is for all designated countries in the following designated countries.
1-6 单独提交的说明  1-6 Instructions submitted separately
这些说明将随后提交给国际局 由受理局填写  These instructions will be subsequently submitted to the International Bureau and filled out by the receiving Office.
0-4 本表格与国际申请一起收到: 0-4 This form was received with the international application:
(是或否)  (Yes or no)
0-4-1 受权官员 由国际局填写  0-4-1 Authorized official Filled in by the International Bureau
0-5 国际局收到本表格日期: 0-5 The International Bureau received the date of this form:
0-5-1 受权官员 0-5-1 authorized official

Claims

权利要求书 Claim
[权利要求 1] 一株凝结芽孢杆菌 Bacillus coagulant ZS-007 , 保藏于中国典型培 养物保藏中心, 保藏编号为 CCTCC M 2015273。  [Claim 1] A Bacillus coagulant ZS-007 is deposited with the China Center for the Conservation of Traditional Cultures under the accession number CCTCC M 2015273.
[权利要求 2] —种权利要求 1所述的凝结芽胞杆菌的高密度发酵方法, 其特征在于 具体步骤如下:  [Claim 2] The high-density fermentation method of Bacillus coagulans according to claim 1, wherein the specific steps are as follows:
( 1 ) 菌种活化  (1) Strain activation
将凝结芽孢杆菌菌种接种至营养琼脂斜面培养基上, 25-37°C下培养 2 4-48hr; 然后划线转接于营养琼脂茄子瓶斜面, 25-37°C下培养 24-48h r; 营养琼脂斜面培养基及营养琼脂茄子瓶的组成均为: 蛋白胨 10 g/L, 牛肉膏 3g/L, 氯化钠 5g/L, 琼脂 15-20g/L, pH7.2-7.4;  The Bacillus coagulans strain was inoculated onto the nutrient agar slant medium, and cultured at 25-37 ° C for 2 4-48 hr; then the streak was transferred to the slant of the nutrient agar eggplant bottle, and cultured at 25-37 ° C for 24-48 h. The composition of nutrient agar slant medium and nutrient agar eggplant bottle are: peptone 10 g / L, beef extract 3g / L, sodium chloride 5g / L, agar 15-20g / L, pH 7.2-7.4;
(2) 摇瓶培养  (2) Shake flask culture
将步骤 (1 ) 得到的菌种接种至摇瓶中, 振荡培养 18-30hr; 摇瓶培养 基配方: 蛋白胨 10 g/L, 牛肉膏 3g/L, 氯化钠  Inoculate the strain obtained in step (1) into a shake flask and shake culture for 18-30 hrs; shake flask culture formula: peptone 10 g/L, beef extract 3 g/L, sodium chloride
5g/L, pH7.2-7.4; 250mL摇瓶装液量为 20mL, 500mL摇瓶装液量为 5 OmL; 培养条件: 摇瓶转速 200r/min, 温度 25-37°C;  5g / L, pH 7.2-7.4; 250mL shake flask volume is 20mL, 500mL shake flask volume is 5 OmL; culture conditions: shake flask speed 200r / min, temperature 25-37 ° C;
(3) 种子罐扩培  (3) Seed tank expansion
种子罐培养基组成: 蛋白胨 10 g/L, 牛肉膏 3g/L, 氯化钠  Seed tank medium composition: peptone 10 g / L, beef extract 3g / L, sodium chloride
5g/L, pH7.2-7.4; 种子罐体积 10- 1000L, 装液量 50-80% ; 培养条件: 搅拌转速 180-250r/min, 通气量 0.5- 1.0vvm, 温度 25-37°C, 培养吋间 1 5g / L, pH 7.2-7.4; seed tank volume 10-1000L, liquid volume 50-80%; culture conditions: stirring speed 180-250r / min, ventilation 0.5-1.0vvm, temperature 25-37 ° C, Training day 1
8-30hr; 8-30hr ;
(4) 发酵罐发酵  (4) Fermentation tank fermentation
以 0.1%- 10%的接种量将步骤 (3) 得到的种子液接入发酵罐, 发酵培 养基组成: 葡萄糖 25 g/L, 蛋白胨 15 g/L, 酵母粉 10 g/L, 磷酸二氢钾 l g/L, 硫酸镁 0.5  The seed liquid obtained in step (3) is connected to the fermenter at an inoculation amount of 0.1% to 10%. The fermentation medium consists of: glucose 25 g/L, peptone 15 g/L, yeast powder 10 g/L, dihydrogen phosphate Potassium lg/L, magnesium sulfate 0.5
g/L, 初始 pH7.0; 发酵罐体积 l-50m 3, 装液量 50-80% ; 培养条件: 搅拌转速 100-200r/min, 通气量 0.5-0.8vvm, 温度 25-37°C, 培养吋间 1 6-48hr; 取发酵液镜检吋, 当 90%以上的菌体都形成芽孢吋, 即到发 酵终点, 得到发酵液。 [权利要求 3] —种基于权利要求 2所述的凝结芽胞杆菌的高密度发酵方法制备干菌 粉的方法, 其特征在于将步骤 (4) 得到的发酵液离心后收集湿菌泥 , 采用喷雾干燥工艺得到干菌粉; 喷雾干燥条件为: 进风温度 210°C , 出风温度 100°C; 干菌粉中活菌数 8.0x10 11 cfu/g以上。 g/L, initial pH7.0; fermenter volume l-50m 3 , liquid loading 50-80%; culture conditions: stirring speed 100-200r/min, aeration 0.5-0.8vvm, temperature 25-37 ° C, The culture was carried out for 16-48 hrs ; the fermentation broth was microscopically examined, and when more than 90% of the cells formed spores, the fermentation broth was obtained. [Claim 3] A method for preparing a dry powder according to the high-density fermentation method of Bacillus coagulans according to claim 2, characterized in that the fermentation liquid obtained in the step (4) is centrifuged, and the wet bacterial sludge is collected, using a spray. The drying process obtains dry powder; the spray drying conditions are: inlet air temperature 210 ° C, air outlet temperature 100 ° C; dry bacteria powder live bacteria number 8.0 x 10 11 cfu / g or more.
PCT/CN2016/090895 2015-07-22 2016-07-21 Bacillus coagulans, high cell density fermentation method thereof, and method for preparing spray-dried powder thereof WO2017012570A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2016297402A AU2016297402B2 (en) 2015-07-22 2016-07-21 Bacillus coagulans, high cell density fermentation method thereof, and method for preparing spray-dried powder thereof

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201510435242.8A CN104974966B (en) 2015-07-22 2015-07-22 A kind of bacillus coagulans and its fermentation process in high density and dry bacterium powder preparation method
CN201510435242.8 2015-07-22

Publications (1)

Publication Number Publication Date
WO2017012570A1 true WO2017012570A1 (en) 2017-01-26

Family

ID=54271933

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2016/090895 WO2017012570A1 (en) 2015-07-22 2016-07-21 Bacillus coagulans, high cell density fermentation method thereof, and method for preparing spray-dried powder thereof

Country Status (3)

Country Link
CN (1) CN104974966B (en)
AU (1) AU2016297402B2 (en)
WO (1) WO2017012570A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109609407A (en) * 2018-12-27 2019-04-12 黄河三角洲京博化工研究院有限公司 It is a kind of for the thermophilic microorganism bacterial strain of mud decrement in situ and its application
CN110117561A (en) * 2019-05-05 2019-08-13 中铁十八局集团有限公司 A kind of increase novel species trees surviving rate composite bacteria agent and preparation method

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104974966B (en) * 2015-07-22 2017-12-12 江南大学 A kind of bacillus coagulans and its fermentation process in high density and dry bacterium powder preparation method
CN105441354B (en) * 2015-10-28 2019-07-02 南京工业大学 A kind of preparation method of high activity bacillus coagulans active bacteria formulation
CN106801013A (en) * 2015-11-26 2017-06-06 瑞普(天津)生物药业有限公司 One kind mixing probiotics dried object and preparation method
CN108184548B (en) * 2016-12-09 2020-07-24 天津农学院 High-density liquid fermentation method for brown mushrooms
CN109207406A (en) * 2018-10-24 2019-01-15 广东绿百多生物开发有限公司 A kind of method and culture medium for improving bacillus coagulans cell and forming gemma
CN109287890B (en) * 2018-11-16 2022-04-19 青岛贝宝海洋科技有限公司 Germination agent-containing bacillus coagulans feed additive for aquaculture and preparation method thereof
CN109593680B (en) * 2018-12-26 2022-02-22 武汉科诺生物科技股份有限公司 Bacillus thuringiensis liquid fermentation medium and bacterial powder and oil suspension agent thereof
CN109943506A (en) * 2019-03-25 2019-06-28 微来世界生物科技(苏州)有限公司 A kind of culture medium and its fermentation process of suitable bacillus coagulans BC01
CN110129230B (en) * 2019-05-20 2020-11-17 江南大学 Microbial preparation and application thereof in domestic sewage treatment of expressway service area
CN110511884B (en) * 2019-07-24 2022-09-20 盛锦合生物科技(江苏)有限公司 Bacillus coagulans and application thereof in feed processing
CN110734873B (en) * 2019-10-10 2022-04-22 华南理工大学 Method for increasing number of bacillus coagulans spores and application
CN110804574A (en) * 2019-12-06 2020-02-18 湖北华扬科技发展有限公司 High-concentration bacillus coagulans liquid fermentation method
CN111296848A (en) * 2020-03-26 2020-06-19 山东正信生物科技股份有限公司 Edible bacillus coagulans powder and preparation process thereof
CN111603489A (en) * 2020-05-28 2020-09-01 武汉微康益生菌研究院有限公司 Microbial inoculum for improving constipation and preparation method thereof
CN111876345A (en) * 2020-06-29 2020-11-03 武汉微康益生菌研究院有限公司 High-density and high-spore conversion rate fermentation method for bacillus coagulans
CN112048450A (en) * 2020-08-14 2020-12-08 润盈生物工程(上海)有限公司 Method for repeatedly fermenting twice by using bacillus coagulans fermentation centrifugal supernatant
CN114645006B (en) * 2020-12-21 2023-09-01 中国科学院微生物研究所 High sugar-tolerant lactic acid production strain and application thereof in D-lactic acid production
CN114437984A (en) * 2022-02-18 2022-05-06 鑫九通科技(武汉)有限公司 Preparation method of lactic acid-producing bacillus coagulans microbial preparation
CN115261260A (en) * 2022-06-16 2022-11-01 漯河微康生物科技有限公司 Fermentation method for improving spore number and stability of bacillus coagulans and preparation method of bacterial powder

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102505003A (en) * 2011-12-19 2012-06-20 湖南省微生物研究所 High-density fermenting method of bacillus coagulans for livestock and poultry, as well as preparation prepared by method and application thereof
CN102943057A (en) * 2012-11-16 2013-02-27 南京工业大学 Bacillus coagulans and process for high-density fermentation of bacillus coagulans
WO2014081395A1 (en) * 2012-11-23 2014-05-30 Agency For Science, Technology And Research Highly Efficient Production Of Lactic Acid From Hemicellulose Sugars By Newly Isolated Thermophilic Bacillus Coagulans Strains
CN104974966A (en) * 2015-07-22 2015-10-14 江南大学 Bacillus coagulans and high-density fermentation method thereof, and dry bacterium powder preparation method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3363438B2 (en) * 2000-05-02 2003-01-08 ビオフェルミン製薬株式会社 Dried bacterial cells by spray drying
CN101412983B (en) * 2008-11-20 2011-01-26 江苏省苏微微生物研究有限公司 Bacillus coagulans, preparation of high-density cultivated spore preparation, and use thereof
CN104232525A (en) * 2014-08-29 2014-12-24 湖北省生物农药工程研究中心 Process for preparing viable bacillus coagulans preparation

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102505003A (en) * 2011-12-19 2012-06-20 湖南省微生物研究所 High-density fermenting method of bacillus coagulans for livestock and poultry, as well as preparation prepared by method and application thereof
CN102943057A (en) * 2012-11-16 2013-02-27 南京工业大学 Bacillus coagulans and process for high-density fermentation of bacillus coagulans
WO2014081395A1 (en) * 2012-11-23 2014-05-30 Agency For Science, Technology And Research Highly Efficient Production Of Lactic Acid From Hemicellulose Sugars By Newly Isolated Thermophilic Bacillus Coagulans Strains
CN104974966A (en) * 2015-07-22 2015-10-14 江南大学 Bacillus coagulans and high-density fermentation method thereof, and dry bacterium powder preparation method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
ZHANG, LIANG ET AL.: "Fermentation and spray drying of Bacillus coagulans to produce spore powder", CHINESE JOURNAL OF BIOPROCESS ENGINEERING, vol. 14, no. 1, 31 January 2016 (2016-01-31), ISSN: 1672-3678 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109609407A (en) * 2018-12-27 2019-04-12 黄河三角洲京博化工研究院有限公司 It is a kind of for the thermophilic microorganism bacterial strain of mud decrement in situ and its application
CN110117561A (en) * 2019-05-05 2019-08-13 中铁十八局集团有限公司 A kind of increase novel species trees surviving rate composite bacteria agent and preparation method
CN110117561B (en) * 2019-05-05 2020-07-28 中铁十八局集团有限公司 Compound biological agent for increasing survival rate of new trees and preparation method

Also Published As

Publication number Publication date
CN104974966A (en) 2015-10-14
AU2016297402A1 (en) 2017-11-02
CN104974966B (en) 2017-12-12
AU2016297402B2 (en) 2019-01-03

Similar Documents

Publication Publication Date Title
WO2017012570A1 (en) Bacillus coagulans, high cell density fermentation method thereof, and method for preparing spray-dried powder thereof
CN107164269B (en) Lactobacillus paracasei, preparation and application of lactobacillus paracasei in pig feed
CN103820363B (en) A kind of preparation and application of faecium bacterium powder
CN106282072B (en) Compound lactobacillus microecological preparation and preparation method and application thereof
CN107034163B (en) Novel pediococcus acidilactici and application thereof
CN112011481B (en) Lactobacillus reuteri for preventing and treating bacterial diarrhea of livestock and poultry and application thereof
CN108373984A (en) A kind of Lactobacillus paracasei and its application
CN108208316B (en) Siamese bacillus-containing feed
CN106047759B (en) One plant of Pediococcus pentosaceus and its application
CN106957810A (en) A kind of Pediococcus acidilactici and application thereof
WO2017012571A1 (en) Use of bacillus coagulans strain in increasing egg production in laying hen
CN107964520A (en) A kind of compound lactobacillus probiotics and preparation method and application
CN104673726A (en) Porcine lactobacillus acidophilus freeze-drying preparation and application thereof
CN102283334A (en) Complex probiotic microcapsule capable of improving intestinal tract micro-ecology of small-sized dogs
CN115094012B (en) Preparation method and application of bacillus coagulans BC-HYC strain microbial inoculum
CN109618552A (en) The method of feed addictive comprising bacillus subtilis and bacillus licheniformis, the fodder compound comprising the feed addictive and the production feed addictive
JP2019524049A (en) Feed additive containing Bacillus subtilis and Bacillus licheniformis, feed composition containing the additive, and method for producing the feed additive
CN107949633B (en) Lactobacillus rhamnosus, animal feed and composition thereof, and production method of inactive cells
CN108546663B (en) Porcine lactobacillus crispatus and application thereof
CN113502243B (en) Lactobacillus plantarum GBW-LP001 capable of highly producing lactic acid and antibacterial agent alternative thereof and application
CN103266074A (en) B.subtilis spores strain and application thereof
CN103255082B (en) One plant of excellent bacillus coagulans and its application for growing and fattening pigs cultivation
CN116179440B (en) Bacillus gallinarum and application thereof
CN114874949B (en) Clostridium butyricum, fermentation product thereof, microbial inoculum containing clostridium butyricum and animal feed additive
CN106811429B (en) Bacillus subtilis strain, application of feed additive thereof and feed

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: 16827261

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2016297402

Country of ref document: AU

Date of ref document: 20160721

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 16827261

Country of ref document: EP

Kind code of ref document: A1