CN102417892B - Feeding lactobacillus johnsonii high-density fermentation medium and application thereof - Google Patents

Feeding lactobacillus johnsonii high-density fermentation medium and application thereof Download PDF

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CN102417892B
CN102417892B CN201110428396.6A CN201110428396A CN102417892B CN 102417892 B CN102417892 B CN 102417892B CN 201110428396 A CN201110428396 A CN 201110428396A CN 102417892 B CN102417892 B CN 102417892B
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lactobacillus johnsonii
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CN102417892A (en
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孙晓雯
汪攀
张军
闫轶洁
王安如
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HARBIN DABEI FARMING AND ANIMAL HUSBANDRY TECHNOLOGY Co Ltd
Hu'nan Dabeinong Agricultural Technology Co Ltd
Jilin Dabeinong Agriculture Animal Husbandry Technology Co Ltd
Beijing Dabeinong Biotechnology Co Ltd
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Hu'nan Dabeinong Agricultural Technology Co Ltd
Beijing Dabeinong Technology Group Co Ltd
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Abstract

本发明属于乳酸菌培养技术领域,涉及一种饲用约氏乳杆菌高密度发酵培养基及其应用。使用本发明的高密度发酵培养基及其发酵方法发酵的约氏乳杆菌,菌体密度较普通发酵显著提高,活菌数不低于1010cfu/ml,较普通MRS培养基培养活菌数提高80倍以上,实现了约氏乳杆菌的高密度发酵;本发明的发酵培养基及其应用也减小了生物量的分离费用,缩短生产周期,从而降低生产成本、提高生产效率。The invention belongs to the technical field of lactic acid bacteria cultivation, and relates to a high-density fermentation medium of Lactobacillus johnsonii for feeding and an application thereof. Lactobacillus johnsonii fermented by using the high-density fermentation medium of the present invention and its fermentation method, the thalline density is significantly improved compared with ordinary fermentation, the number of viable bacteria is not less than 10 10 cfu/ml, and the number of viable bacteria cultured compared with ordinary MRS medium The increase is more than 80 times, and the high-density fermentation of Lactobacillus johnsonii is realized; the fermentation medium and its application of the present invention also reduce the separation cost of biomass, shorten the production cycle, thereby reducing production cost and improving production efficiency.

Description

一种饲用约氏乳杆菌高密度发酵培养基及其应用A kind of feeding Lactobacillus johnsonii high-density fermentation medium and application thereof

技术领域 technical field

本发明属于乳酸菌培养技术领域,涉及一种饲用约氏乳杆菌高密度发酵培养基及其应用。The invention belongs to the technical field of lactic acid bacteria cultivation, and relates to a high-density fermentation medium of Lactobacillus johnsonii for feeding and an application thereof.

背景技术 Background technique

乳酸菌是动物消化道中常有的正常菌,应用该类菌研制益生菌剂的历史最早,此菌已被广泛的应用于发酵食品、动物饲料和保健食品中。Lactic acid bacteria are normal bacteria commonly found in the digestive tract of animals. The history of using this type of bacteria to develop probiotics is the earliest. This bacteria has been widely used in fermented food, animal feed and health food.

约氏乳杆菌(Lactobacillus johnsonii)为乳酸菌中的一种,综合目前关于约氏乳杆菌的文献报道,其对动物的益生功能主要体现在以下两方面,一方面,约氏乳杆菌对动物天然防御系统及免疫机能具有调节作用;另一方面,约氏乳杆菌表现出对动物皮炎的特异性预防作用。Tanaka等发现,灌服约氏乳杆菌的小鼠特异性皮炎(atopic dermatitis,AD)发病率降低,同时可有效抑制小鼠表皮增生。Lactobacillus johnsonii (Lactobacillus johnsonii) is a kind of lactic acid bacteria. Based on the current literature reports about Lactobacillus johnsonii, its beneficial function to animals is mainly reflected in the following two aspects. On the one hand, Lactobacillus johnsonii has a natural defense effect on animals. System and immune function have a regulatory effect; on the other hand, Lactobacillus johnsoni showed a specific preventive effect on animal dermatitis. Tanaka et al. found that the incidence of atopic dermatitis (AD) in mice fed with Lactobacillus johnsonii was reduced, and at the same time, it could effectively inhibit epidermal hyperplasia in mice.

传统的静置发酵法得到的发酵液中菌体的发酵密度较低,约氏乳杆菌活菌数在5-10亿左右,为了得到更多的活菌数,就需要增加生物反应器的体积或增加发酵次数等,从而增加生物量的分离费用,延长生产周期,从而提高生产成本、降低生产效率。The fermentation density of the bacteria in the fermentation liquid obtained by the traditional static fermentation method is low, and the number of viable Lactobacillus johnsonii is about 500-100 million. In order to obtain more viable bacteria, it is necessary to increase the volume of the bioreactor Or increase the number of fermentations, etc., thereby increasing the separation cost of biomass and prolonging the production cycle, thereby increasing production costs and reducing production efficiency.

约氏乳杆菌目前仍难以实现高密度发酵,难以实现的主要问题是发酵培养基及其发酵方法,发酵后期营养物质不足和代谢产物(主要是乳酸)积累抑制菌体生长,导致高密度发酵难以实现。Lactobacillus johnsoni is still difficult to achieve high-density fermentation. The main problem that is difficult to achieve is the fermentation medium and its fermentation method. The lack of nutrients and the accumulation of metabolites (mainly lactic acid) in the later stage of fermentation inhibit the growth of bacteria, making high-density fermentation difficult. accomplish.

发明内容 Contents of the invention

(一)要解决的技术问题(1) Technical problems to be solved

本发明的目的是提供一种饲用约氏乳杆菌高密度发酵培养基。The object of the invention is to provide a high-density fermentation medium for feeding Lactobacillus johnsonii.

本发明的另一目的是提供该高密度发酵培养基在约氏乳杆菌发酵中的应用。Another object of the present invention is to provide the application of the high-density fermentation medium in the fermentation of Lactobacillus johnsonii.

(二)技术方案(2) Technical solution

本发明的目的是通过如下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:

本发明提供一种饲用约氏乳杆菌(Lactobacillus johnsonii)高密度发酵培养基,该培养基的主要组分及其含量如下:葡萄糖20~30g/L、胰蛋白胨10~15g/L、牛肉膏或牛肉粉6~15g/L、酵母粉5~10g/L、K2HPO4 2~3g/L、CH3COONa 5~8g/L、柠檬酸钠2~4g/L、Mg2+水溶性化合物0.2~0.4g/L、Fe2+水溶性化合物0.1~0.2g/L和Mn2+水溶性化合物45~55mg/L。The invention provides a high-density fermentation medium of Lactobacillus johnsonii for feeding. The main components and contents of the medium are as follows: glucose 20-30g/L, tryptone 10-15g/L, beef extract Or beef powder 6~15g/L, yeast powder 5~10g/L, K 2 HPO 4 2~3g/L, CH 3 COONa 5~8g/L, sodium citrate 2~4g/L, Mg 2+ water soluble Compound 0.2-0.4g/L, Fe 2+ water-soluble compound 0.1-0.2g/L and Mn 2+ water-soluble compound 45-55mg/L.

其中,所述的Mg2+水溶性化合物为MgSO4、MgCl2中的任一种;所述的Fe2+水溶性化合物为FeSO4、FeCl2、(NH4)2Fe(SO4)2中的任一种;所述的Mn2+水溶性化合物为MnSO4Wherein, the Mg 2+ water-soluble compound is any one of MgSO 4 and MgCl 2 ; the Fe 2+ water-soluble compound is FeSO 4 , FeCl 2 , (NH 4 ) 2 Fe(SO 4 ) 2 Any one of them; the Mn 2+ water-soluble compound is MnSO 4 .

本发明发酵培养基的配制方法如下:The preparation method of fermentation medium of the present invention is as follows:

(1)按含量分别称取各组分,用蒸馏水溶解,其中葡萄糖单独溶解;(1) Weigh each component according to the content, dissolve with distilled water, wherein glucose is dissolved separately;

(2)葡萄糖115℃单独灭菌20分钟,其它组分装入发酵罐中121℃灭菌30分钟;(2) Glucose is sterilized separately at 115°C for 20 minutes, and other components are put into a fermenter and sterilized at 121°C for 30 minutes;

(3)接种前通过无菌操作将葡萄糖加入发酵罐中,搅拌混匀,即得。(3) Before inoculation, glucose is added into the fermenter through aseptic operation, stirred and mixed evenly, and the obtained product is obtained.

本发明的饲用约氏乳杆菌高密度发酵培养基可以应用于约氏乳杆菌的发酵中,为最大的发挥本发明培养基的效果,使用本发明的培养基发酵约氏乳杆菌时,其发酵过程如下:The high-density fermentation medium of Lactobacillus johnsonii for feeding of the present invention can be applied in the fermentation of Lactobacillus johnsonii, and in order to maximize the effect of the culture medium of the present invention, when using the culture medium of the present invention to ferment Lactobacillus johnsonii, its The fermentation process is as follows:

(1)将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后,以1%接种量转接于MRS液体培养基,培养8~10小时后作为种子液;(1) Activate cryopreserved Lactobacillus johnsonii three times on the MRS agar plate, pick a single colony and inoculate it into the deep MRS liquid test tube, cultivate it at 37°C for 10 hours, transfer it to the MRS liquid medium with 1% inoculation amount, and culture After 8 to 10 hours, it is used as a seed solution;

(2)配制约氏乳杆菌高密度发酵培养基,培养基降至所需温度时,接上溶氧电极,标定溶氧为100%;(2) Prepare a high-density fermentation medium for Lactobacillus johnsonii. When the medium drops to the required temperature, connect a dissolved oxygen electrode, and mark the dissolved oxygen as 100%;

(3)以5%~10%的接种量将步骤(1)所得的种子液接种于步骤(2)的发酵培养基中;(3) inoculating the seed liquid obtained in step (1) in the fermentation medium of step (2) with an inoculation amount of 5% to 10%;

(4)发酵,发酵过程中维持发酵液pH值为6~6.5,当pH超过设定值时,补加料液;当pH低于设定值时,自动流加碱性中和剂氨水、KOH、NaOH中的任一种;在温度37~39℃、转速100rpm条件下发酵10~14小时,发酵过程不通气或通入N2,维持溶氧小于1%;(4) Fermentation, maintain the pH value of the fermentation broth at 6-6.5 during the fermentation process, when the pH exceeds the set value, add feed liquid; when the pH is lower than the set value, automatically add alkaline neutralizer ammonia water, KOH , any one of NaOH; ferment for 10-14 hours at a temperature of 37-39°C and a rotational speed of 100 rpm, without aeration or N 2 during the fermentation process, and maintain dissolved oxygen less than 1%;

(5)当补加料液pH不再降低或发酵液在600nm波长下的吸光值不再增加时,终止发酵,即得约氏乳杆菌活菌数达1010cfu/ml以上的发酵液。(5) When the pH of the added feed liquid no longer decreases or the absorbance value of the fermented liquid no longer increases at 600nm wavelength, the fermentation is terminated, and the fermented liquid with the viable count of Lactobacillus johnsonii reaching more than 10 10 cfu/ml is obtained.

其中,所述料液的主要组分及其含量如下:蔗糖500g/L、蛋白胨150g/L、牛肉粉或牛肉膏150g/L、酵母膏或酵母浸粉75g/L。Wherein, the main components and contents of the feed liquid are as follows: 500 g/L sucrose, 150 g/L peptone, 150 g/L beef powder or beef extract, 75 g/L yeast extract or yeast extract powder.

本发明的高密度发酵培养基及其发酵方法也可应用于其它乳酸菌,但为达到最好的发明效果,优选适用于约氏乳杆菌(Lactobacillusjohnsonii)。The high-density fermentation medium and the fermentation method thereof of the present invention can also be applied to other lactic acid bacteria, but in order to achieve the best inventive effect, it is preferably applicable to Lactobacillus johnsonii.

(三)有益效果(3) Beneficial effects

本发明采用pH反馈控制分批补料发酵策略,同时降低发酵液中乳酸的浓度,从而解除乳酸的反馈抑制作用,使用本发明的高密度发酵培养基及其发酵方法发酵的约氏乳杆菌,菌体密度较普通发酵显著提高,活菌数不低于1010cfu/ml,这是现有的技术难以达到的发酵标准,较普通MRS培养基培养活菌数5.1×108cfu/ml,提高80倍以上,实现了约氏乳杆菌的高密度发酵;本发明的发酵培养基及其应用也减小了生物量的分离费用,缩短生产周期,从而降低生产成本、提高生产效率。The present invention adopts the fed-batch fermentation strategy of pH feedback control, and at the same time reduces the concentration of lactic acid in the fermentation liquid, thereby releasing the feedback inhibition effect of lactic acid, using the high-density fermentation medium and its fermentation method of the present invention to ferment Lactobacillus johnsonii, The cell density is significantly higher than that of ordinary fermentation, and the number of viable bacteria is not less than 10 10 cfu/ml, which is a fermentation standard that is difficult to achieve with existing technologies. Compared with ordinary MRS medium, the number of viable bacteria cultured is 5.1×10 8 cfu/ml, The increase is more than 80 times, and the high-density fermentation of Lactobacillus johnsonii is realized; the fermentation medium and its application of the present invention also reduce the separation cost of biomass, shorten the production cycle, thereby reducing production cost and improving production efficiency.

具体实施方式 Detailed ways

通过下列实施例将更具体的说明本发明,但是应理解所述实施例仅是为了说明本发明,而不是以任何方式限制本发明的范围。The present invention will be described more specifically through the following examples, but it should be understood that the examples are only for illustrating the present invention, not limiting the scope of the present invention in any way.

本发明下列实施例所用的仪器型号、试剂及其来源如下:The used instrument model, reagent and source thereof of the following examples of the present invention are as follows:

发酵罐:NewBrunswick公司BioFlo/Celligen115型;Fermentation tank: BioFlo/Celligen115 type of New Brunswick company;

循环水机:北京长流科学仪器公司DX-208型;Circulating water machine: DX-208 type of Beijing Changliu Scientific Instrument Company;

空气压缩机:北京豪福机电技术开发应用有限公司HF-6100C型;Air compressor: HF-6100C type of Beijing Haofu Electromechanical Technology Development and Application Co., Ltd.;

分光光度计:上海精密科学仪器有限公司721N型;Spectrophotometer: Shanghai Precision Scientific Instrument Co., Ltd. Model 721N;

显微镜:OLYMPUS CX31型;Microscope: OLYMPUS CX31;

超净台:苏净安泰SW-CJ-2FD型;Ultra-clean bench: Sujing Antai SW-CJ-2FD type;

生化培养箱:上海博讯实业有限公司医疗设备厂SPX-250B-Z型Biochemical incubator: Shanghai Boxun Industrial Co., Ltd. Medical Equipment Factory SPX-250B-Z type

酵母膏、牛肉粉、胰蛋白胨购自北京奥博星生物技术责任有限公司,其他试剂均购自北京化学试剂公司。Yeast extract, beef powder, and tryptone were purchased from Beijing Aoboxing Biotechnology Co., Ltd., and other reagents were purchased from Beijing Chemical Reagent Company.

约氏乳杆菌:来源于中国普通微生物菌种保藏管理中心,保藏编号为CGMCC No.4926。Lactobacillus johnsonii: It comes from the China General Microorganism Culture Collection Management Center, and the preservation number is CGMCC No.4926.

实施例1发酵培养基的配制及发酵比较Preparation and fermentation comparison of embodiment 1 fermentation medium

1、约氏乳杆菌高密度发酵培养基组分及其含量为:1. The components and content of Lactobacillus johnsonii high-density fermentation medium are:

葡萄糖:20g/L、胰蛋白胨:10g/L、牛肉膏:10g/L、酵母粉:5g/L、K2HPO4:2g/L、CH3COONa:5g/L、柠檬酸钠:2g/L、MgSO4:0.2g/L、FeSO4:0.1g/L、MnSO4:55mg/L。Glucose: 20g/L, tryptone: 10g/L, beef extract: 10g/L, yeast powder: 5g/L, K 2 HPO 4 : 2g/L, CH 3 COONa: 5g/L, sodium citrate: 2g/L L. MgSO 4 : 0.2g/L, FeSO 4 : 0.1g/L, MnSO 4 : 55mg/L.

2、培养基配制方法:2. Medium preparation method:

(1)按上述含量分别称取各组分,用蒸馏水溶解,其中葡萄糖单独溶解;(1) Weigh each component according to the above-mentioned content, dissolve with distilled water, wherein glucose is dissolved separately;

(2)葡萄糖115℃单独灭菌20分钟,其他组分装入发酵罐中121℃灭菌30分钟;(2) Glucose is sterilized separately at 115°C for 20 minutes, and other components are put into a fermenter and sterilized at 121°C for 30 minutes;

(3)接种前通过无菌操作将葡萄糖加入发酵罐中,搅拌混匀,即得。(3) Before inoculation, glucose is added into the fermenter through aseptic operation, stirred and mixed evenly, and the obtained product is obtained.

3、高密度发酵与现有技术发酵的比较3. Comparison between high-density fermentation and existing technology fermentation

3.1高密度发酵主要步骤如下3.1 The main steps of high-density fermentation are as follows

(1)将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后,以1%接种量转接于MRS液体培养基,培养10小时后作为种子液;(1) Activate cryopreserved Lactobacillus johnsonii three times on the MRS agar plate, pick a single colony and inoculate it into the deep MRS liquid test tube, cultivate it at 37°C for 10 hours, transfer it to the MRS liquid medium with 1% inoculation amount, and culture After 10 hours as a seed solution;

(2)配制发酵培养基,培养基降至所需温度时,接上溶氧电极,标定溶氧为100%;(2) Prepare the fermentation medium, when the medium drops to the required temperature, connect the dissolved oxygen electrode, and mark the dissolved oxygen as 100%;

(3)以5%的接种量将步骤(1)所得的种子液接种于步骤(2)的发酵培养基中;(3) inoculate the seed liquid obtained in step (1) in the fermentation medium of step (2) with an inoculum size of 5%;

(4)发酵,发酵过程中维持发酵液pH值为6.0,当pH超过6.0时,补加料液约100ml;当pH低于6.0时,自动流加碱性中和剂氨水;在温度37℃、转速100rpm条件下发酵10小时,发酵过程不通气,维持溶氧小于1%;(4) Fermentation, maintain the pH value of the fermentation broth at 6.0 during the fermentation process. When the pH exceeds 6.0, add about 100ml of feed liquid; when the pH is lower than 6.0, automatically add alkaline neutralizer ammonia water; Ferment for 10 hours under the condition of rotating speed 100rpm, the fermentation process is not ventilated, and the dissolved oxygen is maintained at less than 1%;

(5)当补加料液pH不再降低时,终止发酵,即得约氏乳杆菌活菌数达4.3×1010cfu/ml的发酵液。(5) When the pH of the added feed liquid no longer decreases, the fermentation is terminated to obtain a fermentation liquid in which the viable count of Lactobacillus johnsonii reaches 4.3×10 10 cfu/ml.

3.2对照实验3.2 Control experiment

(1)约氏乳杆菌发酵培养基(MRS培养基)其组分与含量为:(1) The components and contents of Lactobacillus johnsonii fermentation medium (MRS medium) are:

葡萄糖:20g/L、蛋白胨:10g/L、牛肉膏:5g/L、酵母粉:4g/L、K2HPO4:2g/L、CH3COONa:5g/L、柠檬酸钠:2g/L、MgSO4:0.2g/L、MnSO4:50mg/L、吐温80:1ml。Glucose: 20g/L, peptone: 10g/L, beef extract: 5g/L, yeast powder: 4g/L, K 2 HPO 4 : 2g/L, CH 3 COONa: 5g/L, sodium citrate: 2g/L , MgSO 4 : 0.2g/L, MnSO 4 : 50mg/L, Tween 80: 1ml.

(2)发酵(2) fermentation

将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后。以1%接种量转接于MRS液体培养基,培养10小时后作为种子液,以10%接种量接种发酵培养基。37℃静置培养10小时,终止发酵,得到约氏乳杆菌活菌数为5.1×108cfu/ml。The cryopreserved Lactobacillus johnsonii was activated three times on the MRS agar plate, and a single colony was picked and inoculated into the deep MRS liquid test tube, and cultured at 37°C for 10 hours. Transfer to MRS liquid medium with 1% inoculum amount, cultivate for 10 hours as seed liquid, and inoculate fermentation medium with 10% inoculum amount. After static culture at 37°C for 10 hours, the fermentation was terminated, and the viable count of Lactobacillus johnsonii was 5.1×10 8 cfu/ml.

3.3结果分析3.3 Result analysis

应用本发明的培养基及其发酵方法,可以得到约氏乳杆菌活菌数达4.3×1010cfu/ml的发酵液,而应用现行发酵培养基(MRS培养基)及其发酵方法,得到的约氏乳杆菌活菌数仅为5.1×108cfu/ml。实验证明本发明的培养基及其发酵方法得到的约氏乳杆菌活菌数为现有技术的近80倍,实现了约氏乳杆菌的高密度发酵。Apply the culture medium of the present invention and its fermentation method, can obtain the fermented liquid that the Lactobacillus johnsonii viable count reaches 4.3×10 10 cfu/ml, and apply current fermentation culture medium (MRS culture medium) and its fermentation method, obtain The viable count of Lactobacillus johnsonii was only 5.1×10 8 cfu/ml. Experiments have proved that the number of viable Lactobacillus johnsonii obtained by the medium and the fermentation method of the present invention is nearly 80 times that of the prior art, and high-density fermentation of Lactobacillus johnsonii has been realized.

实施例2发酵培养基的配制及发酵比较Preparation and fermentation comparison of embodiment 2 fermentation medium

1、约氏乳杆菌高密度发酵培养基其组分与含量为:1. The components and contents of Lactobacillus johnsonii high-density fermentation medium are:

葡萄糖:25g/L、胰蛋白胨:10g/L、牛肉粉:15g/L、酵母粉:10g/L、K2HPO4:2g/L、CH3COONa:7g/L、柠檬酸钠:3g/L、MgCl2:0.2g/L、FeCl2:0.1g/L、MnSO4:50mg/L。Glucose: 25g/L, tryptone: 10g/L, beef powder: 15g/L, yeast powder: 10g/L, K 2 HPO 4 : 2g/L, CH 3 COONa: 7g/L, sodium citrate: 3g/L L, MgCl 2 : 0.2g/L, FeCl 2 : 0.1g/L, MnSO 4 : 50mg/L.

2、培养基配制方法:2. Medium preparation method:

(1)按含量分别称取各组分,用蒸馏水溶解,其中葡萄糖单独溶解;(1) Weigh each component according to the content, dissolve with distilled water, wherein glucose is dissolved separately;

(2)葡萄糖115℃单独灭菌20分钟,其他组分装入发酵罐中121℃灭菌30分钟;(2) Glucose is sterilized separately at 115°C for 20 minutes, and other components are put into a fermenter and sterilized at 121°C for 30 minutes;

(3)接种前通过无菌操作将葡萄糖加入发酵罐中,搅拌混匀,即得。3、高密度发酵与现有技术发酵的比较(3) Before inoculation, glucose is added into the fermenter through aseptic operation, stirred and mixed evenly, and the obtained product is obtained. 3. Comparison between high-density fermentation and existing technology fermentation

3.1高密度发酵主要步骤如下3.1 The main steps of high-density fermentation are as follows

(1)将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后,以1%接种量转接于MRS液体培养基,培养8小时后作为种子液;(1) Activate cryopreserved Lactobacillus johnsonii three times on the MRS agar plate, pick a single colony and inoculate it into the deep MRS liquid test tube, cultivate it at 37°C for 10 hours, transfer it to the MRS liquid medium with 1% inoculation amount, and culture 8 hours later as seed liquid;

(2)配制发酵培养基,培养基降至所需温度时,接上溶氧电极,标定溶氧为100%;(2) Prepare the fermentation medium, when the medium drops to the required temperature, connect the dissolved oxygen electrode, and mark the dissolved oxygen as 100%;

(3)以5%的接种量将步骤(1)所得的种子液接种于步骤(2)的发酵培养基中;(3) inoculate the seed liquid obtained in step (1) in the fermentation medium of step (2) with an inoculum size of 5%;

(4)发酵,发酵过程中维持发酵液pH值为6.3,当pH超过设定值时,补加料液约100ml;当pH低于设定值时,自动流加碱性中和剂氨水;在温度38℃、转速100rpm条件下发酵12小时,发酵过程不通气,维持溶氧小于1%;(4) Fermentation. During the fermentation process, the pH value of the fermented liquid is maintained at 6.3. When the pH exceeds the set value, about 100ml of feed liquid is added; when the pH is lower than the set value, the alkaline neutralizer ammonia water is automatically added; Ferment for 12 hours at a temperature of 38°C and a rotation speed of 100 rpm, without ventilation during the fermentation process, and maintain dissolved oxygen less than 1%;

(5)当补加料液发酵液OD600不再增加时,终止发酵,即得约氏乳杆菌活菌数达5.9×1010cfu/ml的发酵液。(5) When the OD 600 of the fermented liquid of the added feed liquid does not increase any more, the fermentation is terminated, and the fermented liquid in which the viable count of Lactobacillus johnsonii reaches 5.9×10 10 cfu/ml is obtained.

3.2对照实验:3.2 Control experiment:

(1)约氏乳杆菌发酵培养基(MRS培养基)其组分与含量为:(1) The components and content of Lactobacillus johnsonii fermentation medium (MRS medium) are:

葡萄糖:20g/L、蛋白胨:10g/L、牛肉粉:5g/L、酵母粉:4g/L、K2HPO4:2g/L、CH3COONa:5g/L、柠檬酸钠:2g/L、MgSO4:0.2g/L、MnSO4:50mg/L、吐温80:1ml。Glucose: 20g/L, peptone: 10g/L, beef powder: 5g/L, yeast powder: 4g/L, K 2 HPO 4 : 2g/L, CH 3 COONa: 5g/L, sodium citrate: 2g/L , MgSO 4 : 0.2g/L, MnSO 4 : 50mg/L, Tween 80: 1ml.

(2)发酵:(2) Fermentation:

将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后。以1%接种量转接于MRS液体培养基,培养10小时后作为种子液,以10%接种量接种发酵培养基。38℃静置培养12小时,终止发酵,得到所述约氏乳杆菌活菌数为6.0×108cfu/ml。The cryopreserved Lactobacillus johnsonii was activated three times on the MRS agar plate, and a single colony was picked and inoculated into the deep MRS liquid test tube, and cultured at 37°C for 10 hours. Transfer to MRS liquid medium with 1% inoculum amount, cultivate for 10 hours as seed liquid, and inoculate fermentation medium with 10% inoculum amount. Static culture was carried out at 38°C for 12 hours, and the fermentation was terminated, and the number of viable Lactobacillus johnsonii was 6.0×10 8 cfu/ml.

3.3结果分析3.3 Result analysis

应用本发明的培养基及其发酵方法,可以得到约氏乳杆菌活菌数达5.9×1010cfu/ml的发酵液,而应用现行发酵培养基(MRS培养基)及其发酵方法,得到的约氏乳杆菌活菌数仅为6.0×108cfu/ml。实验证明本发明的培养基及其发酵方法得到的约氏乳杆菌活菌数为现有技术的98倍,实现了约氏乳杆菌的高密度发酵。Applying the culture medium of the present invention and its fermentation method, can obtain the fermented liquid that the Lactobacillus johnsonii viable count reaches 5.9×10 10 cfu/ml, and apply the current fermentation culture medium (MRS culture medium) and its fermentation method, obtain The viable count of Lactobacillus johnsonii is only 6.0×10 8 cfu/ml. Experiments have proved that the number of viable Lactobacillus johnsonii obtained by the culture medium and the fermentation method of the present invention is 98 times that of the prior art, and high-density fermentation of Lactobacillus johnsonii has been realized.

实施例3发酵培养基的配制及发酵比较Preparation and fermentation comparison of embodiment 3 fermentation medium

1、约氏乳杆菌高密度发酵培养基其组分与含量为:1. The components and contents of Lactobacillus johnsonii high-density fermentation medium are:

葡萄糖:30g/L、胰蛋白胨:15g/L、牛肉膏:6g/L、酵母粉:6g/L、K2HPO4:3g/L、CH3COONa:8g/L、柠檬酸钠:4g/L、(NH4)2Fe(SO4)2:0.2g/L、MgSO4:0.4g/L、MnSO4:45mg/L。Glucose: 30g/L, tryptone: 15g/L, beef extract: 6g/L, yeast powder: 6g/L, K 2 HPO 4 : 3g/L, CH 3 COONa: 8g/L, sodium citrate: 4g/L L, (NH 4 ) 2 Fe(SO 4 ) 2 : 0.2 g/L, MgSO 4 : 0.4 g/L, MnSO 4 : 45 mg/L.

2、培养基配制方法:2. Medium preparation method:

(1)按含量分别称取各组分,用蒸馏水溶解,其中葡萄糖单独溶解;(1) Weigh each component according to the content, dissolve with distilled water, wherein glucose is dissolved separately;

(2)葡萄糖115℃单独灭菌20分钟,其他组分装入发酵罐中121℃灭菌30分钟;(2) Glucose is sterilized separately at 115°C for 20 minutes, and other components are put into a fermenter and sterilized at 121°C for 30 minutes;

(3)接种前通过无菌操作将葡萄糖加入发酵罐中,搅拌混匀,即得。(3) Before inoculation, glucose is added into the fermenter through aseptic operation, stirred and mixed evenly, and the obtained product is obtained.

3、高密度发酵与现有技术发酵的比较3. Comparison between high-density fermentation and existing technology fermentation

3.1高密度发酵主要步骤如下3.1 The main steps of high-density fermentation are as follows

(1)将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后,以1%接种量转接于MRS液体培养基,培养10小时后作为种子液;(1) Activate cryopreserved Lactobacillus johnsonii three times on the MRS agar plate, pick a single colony and inoculate it into the deep MRS liquid test tube, cultivate it at 37°C for 10 hours, transfer it to the MRS liquid medium with 1% inoculation amount, and culture After 10 hours as a seed solution;

(2)配制发酵培养基,培养基降至所需温度时,接上溶氧电极,标定溶氧为100%;(2) Prepare the fermentation medium, when the medium drops to the required temperature, connect the dissolved oxygen electrode, and mark the dissolved oxygen as 100%;

(3)以10%的接种量将步骤(1)所得的种子液接种于步骤(2)的发酵培养基中;(3) inoculate the seed liquid obtained in step (1) in the fermentation medium of step (2) with an inoculum size of 10%;

(4)发酵,发酵过程中维持发酵液pH值为6.5,当pH超过设定值时,补加料液约100ml;当pH低于设定值时,自动流加碱性中和剂氨水;在温度39℃、转速100rpm条件下发酵14小时,发酵过程通入氮气,维持溶氧小于1%;(4) Fermentation, maintain the pH value of the fermented liquid during the fermentation process at 6.5, when the pH exceeds the set value, add about 100ml of feed liquid; when the pH is lower than the set value, automatically add alkaline neutralizer ammonia water; Ferment for 14 hours at a temperature of 39°C and a rotation speed of 100 rpm, nitrogen gas is introduced during the fermentation process, and dissolved oxygen is maintained at less than 1%;

(5)当补加料液pH不再降低时,终止发酵,即得约氏乳杆菌活菌数达4.9×1010cfu/ml的发酵液。(5) When the pH of the added feed liquid no longer decreases, the fermentation is terminated, and the fermentation liquid in which the viable count of Lactobacillus johnsonii reaches 4.9×10 10 cfu/ml is obtained.

3.2对照实验:3.2 Control experiment:

(1)约氏乳杆菌发酵培养基(MRS培养基)其组分为:(1) The components of Lactobacillus johnsonii fermentation medium (MRS medium) are:

葡萄糖:20g/L、蛋白胨:10g/L、牛肉膏:5g/L、酵母粉:4g/L、K2HPO4:2g/L、CH3COONa:5g/L、柠檬酸钠:2g/L、MgSO4:0.2g/L、MnSO4:50mg/L、吐温80:1ml。Glucose: 20g/L, peptone: 10g/L, beef extract: 5g/L, yeast powder: 4g/L, K 2 HPO 4 : 2g/L, CH 3 COONa: 5g/L, sodium citrate: 2g/L , MgSO 4 : 0.2g/L, MnSO 4 : 50mg/L, Tween 80: 1ml.

(2)发酵(2) fermentation

将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后。以1%接种量转接于MRS液体培养基,培养10小时后作为种子液,以10%接种量接种发酵培养基。39℃静置培养14小时,终止发酵,得到约氏乳杆菌活菌数为4.8×108cfu/ml。The cryopreserved Lactobacillus johnsonii was activated three times on the MRS agar plate, and a single colony was picked and inoculated into the deep MRS liquid test tube, and cultured at 37°C for 10 hours. Transfer to MRS liquid medium with 1% inoculum amount, cultivate for 10 hours as seed liquid, and inoculate fermentation medium with 10% inoculum amount. After static culture at 39°C for 14 hours, the fermentation was terminated, and the viable count of Lactobacillus johnsonii was 4.8×10 8 cfu/ml.

3.3结果分析3.3 Result analysis

应用本发明的培养基及其发酵方法,可以得到约氏乳杆菌活菌数达4.9×1010cfu/ml的发酵液,而应用现行发酵培养基(MRS培养基)及其发酵方法,得到的约氏乳杆菌活菌数仅为4.8×108cfu/ml。实验证明本发明的培养基及其发酵方法得到的约氏乳杆菌活菌数为现有技术的近102倍,实现了约氏乳杆菌的高密度发酵。生产中,高密度发酵的实现可以减小生物量的分离费用,缩短生产周期,降低生产成本、提高生产效率等,这在高效节能的当代社会具有极其重要的意义。Apply the culture medium of the present invention and its fermentation method, can obtain the fermented liquid that the number of live bacteria of Lactobacillus johnsonii reaches 4.9×10 10 cfu/ml, and apply the current fermentation culture medium (MRS culture medium) and its fermentation method, obtain The viable count of Lactobacillus johnsonii was only 4.8×10 8 cfu/ml. Experiments have proved that the number of viable Lactobacillus johnsonii obtained by the medium and the fermentation method of the present invention is nearly 102 times that of the prior art, and high-density fermentation of Lactobacillus johnsonii has been realized. In production, the realization of high-density fermentation can reduce the cost of biomass separation, shorten the production cycle, reduce production costs, improve production efficiency, etc., which is of great significance in the contemporary society of high efficiency and energy saving.

Claims (2)

1.一种饲用约氏乳杆菌(Lactobacillus johnsonii)CGMCC No.4926高密度发酵方法,其特征在于,发酵过程如下: 1. Lactobacillus johnsonii (Lactobacillus johnsonii) CGMCC No.4926 high-density fermentation method for feeding is characterized in that the fermentation process is as follows: (1)将冷冻保存的约氏乳杆菌在MRS琼脂平板活化三次,挑取单菌落接种于深层MRS液体试管,37℃培养10小时后,以1%接种量转接于MRS液体培养基,培养8~10小时后作为种子液; (1) Activate cryopreserved Lactobacillus johnsonii three times on the MRS agar plate, pick a single colony and inoculate it into the deep MRS liquid test tube, cultivate it at 37°C for 10 hours, transfer it to the MRS liquid medium with 1% inoculation amount, and culture After 8 to 10 hours, it is used as a seed solution; (2)配制高密度发酵培养基,培养基降至所需温度时,接上溶氧电极,标定溶氧为100%; (2) Prepare a high-density fermentation medium, when the medium drops to the required temperature, connect the dissolved oxygen electrode, and mark the dissolved oxygen as 100%; (3)以5%~10%的接种量将步骤(1)所得的种子液接种于步骤(2)的发酵培养基中; (3) inoculating the seed liquid obtained in step (1) in the fermentation medium of step (2) with an inoculation amount of 5% to 10%; (4)发酵,发酵过程中维持发酵液pH值为6~6.5,当pH超过设定值时,补加料液;当pH低于设定值时,自动流加碱性中和剂氨水、KOH、NaOH中的任一种;在温度37~39℃、转速100rpm条件下发酵10~14小时,发酵过程不通气或通入N2,维持溶氧小于1%; (4) Fermentation, maintain the pH value of the fermentation broth at 6-6.5 during the fermentation process, when the pH exceeds the set value, add feed liquid; when the pH is lower than the set value, automatically add alkaline neutralizer ammonia water, KOH , any one of NaOH; ferment for 10-14 hours at a temperature of 37-39°C and a rotational speed of 100 rpm, without aeration or N 2 during the fermentation process, and maintain dissolved oxygen less than 1%; (5)当补加料液pH不再降低或发酵液在600nm波长下的吸光值不再增加时,终止发酵,即得约氏乳杆菌活菌数达1010cfu/ml以上的发酵液, (5) When the pH of the added feed liquid no longer decreases or the absorbance value of the fermented liquid no longer increases at 600nm wavelength, the fermentation is terminated, and the fermented liquid in which the viable count of Lactobacillus johnsonii reaches more than 10 cfu/ml is obtained, 其中,所述的高密度发酵培养基的主要组分及其含量如下:葡萄糖20~30g/L、胰蛋白胨10~15g/L、牛肉膏或牛肉粉6~15g/L、酵母粉5~10g/L、K2HPO4 2~3g/L、CH3COONa 5~8g/L、柠檬酸钠2~4g/L、Mg2+水溶性化合物0.2~0.4g/L、Fe2+水溶性化合物0.1~0.2g/L和Mn2+水溶性化合物45~55mg/L, Wherein, the main components and contents of the high-density fermentation medium are as follows: glucose 20-30g/L, tryptone 10-15g/L, beef extract or beef powder 6-15g/L, yeast powder 5-10g /L, K 2 HPO 4 2~3g/L, CH 3 COONa 5~8g/L, Sodium citrate 2~4g/L, Mg 2+ water soluble compound 0.2~0.4g/L, Fe 2+ water soluble compound 0.1~0.2g/L and Mn 2+ water-soluble compound 45~55mg/L, 其中,所述料液的主要组分及其含量如下:蔗糖500g/L、蛋白胨150g/L、牛肉粉或牛肉膏150g/L、酵母膏或酵母浸粉75g/L。 Wherein, the main components and contents of the feed liquid are as follows: 500 g/L sucrose, 150 g/L peptone, 150 g/L beef powder or beef extract, 75 g/L yeast extract or yeast extract powder. 2.如权利要求1所述的高密度发酵方法,其特征在于,所述的Mg2+水溶性化合物为MgSO4、MgCl2中的任一种;所述的Fe2+水溶性化合物为FeSO4、FeCl2、(NH4)2Fe(SO4)2中的任一种;所述的Mn2+水溶性化合物为MnSO42. The high-density fermentation method according to claim 1, characterized in that, the Mg 2+ water-soluble compound is any one of MgSO 4 , MgCl 2 ; the Fe 2+ water-soluble compound is FeSO 4. Any one of FeCl 2 , (NH 4 ) 2 Fe(SO 4 ) 2 ; the Mn 2+ water-soluble compound is MnSO 4 . 3. 如权利要求1或2所述的高密度发酵方法,其特征在于,发酵培养基的配制方法如下: 3. The high-density fermentation method as claimed in claim 1 or 2, wherein the preparation method of the fermentation medium is as follows: (1)按含量分别称取各组分,用蒸馏水溶解,其中葡萄糖单独溶解; (1) Weigh each component according to the content, dissolve with distilled water, wherein glucose is dissolved separately; (2)葡萄糖115℃单独灭菌20分钟,其它组分装入发酵罐中121℃灭菌30分钟; (2) Glucose is sterilized separately at 115°C for 20 minutes, and other components are put into a fermenter and sterilized at 121°C for 30 minutes; (3)接种前通过无菌操作将葡萄糖加入发酵罐中,搅拌混匀,即得。 (3) Before inoculation, glucose is added into the fermenter through aseptic operation, stirred and mixed evenly, and the obtained product is obtained.
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