CN106434465B - Method for realizing high-density fermentation of lactic acid bacteria by adopting amorphous solid attachments - Google Patents

Method for realizing high-density fermentation of lactic acid bacteria by adopting amorphous solid attachments Download PDF

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CN106434465B
CN106434465B CN201610892909.1A CN201610892909A CN106434465B CN 106434465 B CN106434465 B CN 106434465B CN 201610892909 A CN201610892909 A CN 201610892909A CN 106434465 B CN106434465 B CN 106434465B
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杜新永
郭兴峰
王雷
李燕
孙小凡
曾庆华
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Liaocheng University
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Abstract

本发明公开了一种采用不定型固体附着物实现乳酸菌高密度发酵的技术,包括以下步骤:(1)选择长势旺盛,并且保证接种后能够在4‑8h达到完成对数生长期的优良乳酸菌菌种进行活化,将活化后的乳酸菌菌种接种于乳酸菌培养基中;(2)于37℃进行发酵培养,培养完成后,收获菌体,即可。本发明提供的发酵技术无需补料,可以一次性完成发酵过程;可以采用一般性发酵罐,无需投资专用发酵罐;本发明可以获得乳酸菌菌体,所有以乳酸菌生物量为发酵目的的生产过程均可以应用;在发酵结束后,菌落总数可以达到1010‑12cfu/mL;所得菌体耐高温、抗逆性强,在模拟胃酸、胆盐环境中存活率提高2‑3倍。The invention discloses a technology for realizing high-density fermentation of lactic acid bacteria by using amorphous solid attachments. (2) Fermentation culture is carried out at 37°C, and after the culture is completed, the cells are harvested. The fermentation technology provided by the invention does not require feeding, and can complete the fermentation process at one time; a general fermenter can be used, and no special fermenter needs to be invested; the invention can obtain lactic acid bacteria cells, and all production processes using lactic acid bacteria biomass as the purpose of fermentation are It can be applied; after the fermentation, the total number of bacterial colonies can reach 10 10-12 cfu/mL; the obtained bacterial cells are resistant to high temperature and stress, and the survival rate is increased by 2-3 times in the simulated gastric acid and bile salt environment.

Description

一种采用不定型固体附着物实现乳酸菌高密度发酵的方法A kind of method that adopts amorphous solid attachment to realize lactic acid bacteria high-density fermentation

技术领域technical field

本发明涉及食品微生物发酵工程领域,特别是涉及一种采用不定型固体附着物实现乳酸菌高密度发酵的方法。The invention relates to the field of food microorganism fermentation engineering, in particular to a method for realizing high-density fermentation of lactic acid bacteria by using amorphous solid attachments.

背景技术Background technique

乳酸菌,是指一群能利用可发酵性碳水化合物,产生大量乳酸的革兰氏阳性细菌的通称。乳酸菌是一类对人体有益的微生物菌群,而且广泛分布在自然界。乳酸菌发酵能够产生大量的有机酸、醇类及各种氨基酸等代谢物,具有抑制腐败均、提高消化率、防癌等生理功效。乳酸菌的应用历史非常悠久,如今广泛应用于发酵乳制品行业、食品加工业、饲料调制、医药卫生以及禽畜疾病的防治。Lactic acid bacteria is a general term for a group of Gram-positive bacteria that can utilize fermentable carbohydrates to produce large amounts of lactic acid. Lactic acid bacteria are a kind of microbial flora that are beneficial to the human body and are widely distributed in nature. The fermentation of lactic acid bacteria can produce a large amount of metabolites such as organic acids, alcohols and various amino acids, which have physiological effects such as inhibiting spoilage, improving digestibility, and preventing cancer. Lactic acid bacteria have a long history of application, and are now widely used in the fermented dairy industry, food processing industry, feed preparation, medicine and health, and the prevention and control of livestock diseases.

随着我国发酵乳制品工业的迅猛发展,积极研究并大力开发高效浓缩型酸奶发酵剂,对于推动我国乳酸菌发酵剂产业化进程,促进我国发酵乳制品工业的发展,具有重要的意义。而乳酸菌超浓缩发酵剂制备的关键是要实现对其高活性、高密度的培养,因此乳酸菌高密度培养工程技术研究具有重要的现实意义和广阔前景。With the rapid development of my country's fermented dairy product industry, active research and vigorous development of high-efficiency concentrated yogurt starter is of great significance for promoting the industrialization of lactic acid bacteria starter in my country and the development of my country's fermented dairy product industry. The key to the preparation of lactic acid bacteria super-concentrated starter is to realize its high activity and high density culture. Therefore, the research on high density culture engineering technology of lactic acid bacteria has important practical significance and broad prospects.

乳酸菌高密度培养可以用来生产发酵剂、益生菌制剂、乳酸、细菌素,以及其他产物等,但乳酸菌在培养过程中的发酵液的酸化及代谢产物会抑制乳酸菌的生长,导致培养的菌体密度及生物量积累的连续性受到严重阻遏。High-density culture of lactic acid bacteria can be used to produce starter, probiotic preparations, lactic acid, bacteriocins, and other products, but the acidification of the fermentation broth and metabolites of lactic acid bacteria during the culture process will inhibit the growth of lactic acid bacteria, resulting in cultured bacteria. Continuity of density and biomass accumulation is severely hindered.

菌体培养过程中,产物抑制系数影响生长速率及产物转化率。而控制pH值的变化仅能部分地减缓这种抑制。现有技术中,为了实现乳酸菌的高密度发酵,可以采用(1)补料、增加膜过滤装置来稀释或去除代谢废物,解除生长抑制;也可以采取(2)固定化或微胶囊化来固定细胞,防止代谢物影响到乳酸菌的生长。另外,还可以采用(3)生物膜诱导法,通过外源刺激使乳酸菌形成生物膜,实现高密度培养;最后,也有学者通过(4)数学模型观察细胞生长周期并计算出细胞浓度的变化趋势、生物合成活力,以及底物消耗率等,最终获得最佳目的物生产模型或高密度培养。In the process of bacterial culture, the product inhibition coefficient affects the growth rate and product conversion rate. Controlling changes in pH only partially mitigated this inhibition. In the prior art, in order to achieve high-density fermentation of lactic acid bacteria, (1) feeding and adding a membrane filtration device can be used to dilute or remove metabolic waste to relieve growth inhibition; (2) immobilization or microencapsulation can also be used to fix cells, preventing metabolites from affecting the growth of lactic acid bacteria. In addition, (3) biofilm induction method can also be used to make lactic acid bacteria form biofilms through exogenous stimulation to achieve high-density culture; finally, some scholars observe the cell growth cycle through (4) mathematical model and calculate the change trend of cell concentration , biosynthetic activity, and substrate consumption rate, etc., and finally obtain the best target production model or high-density culture.

发明内容SUMMARY OF THE INVENTION

针对现有技术存在的不足,本发明的目的在于提供一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,采用无定型固体悬浮物诱导乳酸菌产生生物膜,从而实现乳酸菌的高密度培养。In view of the deficiencies in the prior art, the object of the present invention is to provide a method for realizing high-density fermentation of lactic acid bacteria by adopting amorphous solid attachments, and adopting amorphous solid suspensions to induce lactic acid bacteria to produce biofilm, thereby realizing the high-density cultivation of lactic acid bacteria.

为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:

一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,包括以下步骤:A method for realizing high-density fermentation of lactic acid bacteria using amorphous solid attachments, comprising the following steps:

(1)选择长势旺盛,并且保证接种后能够在4-8h达到完成对数生长期的优良乳酸菌菌种进行活化,将活化后的乳酸菌菌种接种于乳酸菌培养基中;(1) Select the excellent lactic acid bacteria strains that grow vigorously and ensure that they can reach the logarithmic growth phase within 4-8 hours after inoculation for activation, and inoculate the activated lactic acid bacteria strains in the lactic acid bacteria medium;

(2)于37℃进行发酵培养,培养完成后,收获菌体,即可。(2) Fermentation culture is carried out at 37°C, and after the culture is completed, the cells are harvested.

上述一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,优选的方案是,步骤(1)所述乳酸菌菌种是唾液乳杆菌、发酵乳杆菌和乳酸片球菌中的一种。In the above-mentioned method for realizing high-density fermentation of lactic acid bacteria by using unshaped solid attachments, a preferred solution is that the lactic acid bacteria strain in step (1) is one of Lactobacillus salivarius, Lactobacillus fermentum and Pediococcus lactis.

上述一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,优选的方案是,步骤(1)所述乳酸菌菌种的接种量为0.5~1%。In the above-mentioned method for realizing high-density fermentation of lactic acid bacteria by using unshaped solid attachments, a preferred solution is that the inoculum of the lactic acid bacteria strain described in step (1) is 0.5-1%.

上述一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,优选的方案是,步骤(1)所述乳酸菌培养基为PY培养基。In the above-mentioned method for realizing high-density fermentation of lactic acid bacteria by using amorphous solid attachments, a preferred solution is that the lactic acid bacteria medium in step (1) is a PY medium.

上述一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,优选的方案是,所述PY培养基由以下重量组分的原料组成:未水解大分子蛋白质50g,蛋白胨5g,胰蛋白胨5g,酵母粉10g,无水乙酸钠20g,KH2PO4 6g,MgSO4∙7H2O 0.6g,MnSO4∙4H2O 0.2g,水1000 g。Above-mentioned a kind of method that adopts amorphous solid attachment to realize lactic acid bacteria high-density fermentation, preferred scheme is, described PY medium is made up of the raw material of following weight components: unhydrolyzed macromolecular protein 50g, peptone 5g, tryptone 5g, Yeast powder 10g, anhydrous sodium acetate 20g, KH 2 PO 4 6g, MgSO 4 ∙7H 2 O 0.6g, MnSO 4 ∙4H 2 O 0.2g, water 1000g.

上述一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,优选的方案是,所述PY培养基的pH为6.8。In the above-mentioned method for realizing high-density fermentation of lactic acid bacteria by using amorphous solid attachments, a preferred solution is that the pH of the PY medium is 6.8.

上述一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,优选的方案是,步骤(2)所述发酵的时间为36-48h。In the above-mentioned method for realizing high-density fermentation of lactic acid bacteria by using amorphous solid attachments, a preferred solution is that the fermentation time in step (2) is 36-48 hours.

与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:

(1) 本发明提供的发酵方法无需补料,可以一次性完成发酵过程;可以采用一般性发酵罐,无需投资专用发酵罐;(1) The fermentation method provided by the present invention does not require feeding materials, and can complete the fermentation process at one time; a general fermentation tank can be used, and there is no need to invest in a special fermentation tank;

(2)本发明可以获得乳酸菌菌体,所有以乳酸菌生物量为发酵目的的生产过程均可以应用,而固定化(生物膜)的高密度培养方法无法获得乳酸菌菌体,只能以乳酸菌代谢物作为目标产物;(2) The present invention can obtain lactic acid bacteria cells, and all production processes with lactic acid bacteria biomass as the purpose of fermentation can be applied, and the high-density culture method of immobilization (biofilm) cannot obtain lactic acid bacteria cells, only lactic acid bacteria metabolites can be used. as the target product;

(3)本发明提供的发酵方法,在发酵结束后,菌落总数可以达到1010-12 cfu/mL;获得的发酵剂由酸凝蛋白包裹,实现了大部分的菌体包埋;(3) In the fermentation method provided by the present invention, after the fermentation, the total number of bacterial colonies can reach 10 10-12 cfu/mL; the obtained starter is wrapped by acid curdling protein, and most of the bacterial cells are embedded;

(4)由本发明发酵方法获得的菌体耐高温、抗逆性强,在模拟胃酸、胆盐环境中存活率提高2-3倍。(4) The bacteria obtained by the fermentation method of the present invention have high temperature resistance and strong stress resistance, and the survival rate is increased by 2-3 times in the simulated gastric acid and bile salt environment.

附图说明Description of drawings

图1-3显示为本发明和对照组发酵方法所得菌落总数的对比图。Figures 1-3 show the comparison of the total number of colonies obtained by the fermentation method of the present invention and the control group.

图4-6显示为本发明和对照组发酵产物的耐高温对比图。Figures 4-6 show a comparison chart of the high temperature resistance of the fermentation products of the present invention and the control group.

图7-9显示为本发明和对照组发酵产物的胃酸耐受力对比图。Figures 7-9 are graphs showing the comparison of gastric acid tolerance of the fermentation products of the present invention and the control group.

图10-12显示为本发明和对照组发酵产物的胆盐耐受力对比图。Figures 10-12 are graphs showing the comparison of bile salt tolerance of the fermentation products of the present invention and the control group.

具体实施方式Detailed ways

下面结合实施例和实验例详细说明本发明的技术方案,但保护范围不限于此。本发明所用原料皆可从市场购买。The technical solutions of the present invention will be described in detail below with reference to the embodiments and experimental examples, but the protection scope is not limited thereto. The raw materials used in the present invention can be purchased from the market.

实施例1 一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,包括以下步骤:Embodiment 1 A method for realizing high-density fermentation of lactic acid bacteria by using unshaped solid attachments, comprising the following steps:

(1)选择长势旺盛,并且保证接种后能够在4-8h达到完成对数生长期的优良唾液乳杆菌菌种进行活化,将活化后的唾液乳杆菌菌种接种于pH为6.8的PY培养基中,所述唾液乳杆菌菌种的接种量为0.5~1%,所述PY培养基由以下重量组分的原料组成:未水解大分子蛋白质50g,蛋白胨5g,胰蛋白胨5g,酵母粉10g,无水乙酸钠20g,KH2PO4 6g,MgSO4∙7H2O0.6g,MnSO4∙4H2O 0.2g,水1000g;(1) Select excellent Lactobacillus salivarius strains that grow vigorously and ensure that they can reach the logarithmic growth phase within 4-8 hours after inoculation for activation, and inoculate the activated Lactobacillus salivarius strains in PY medium with a pH of 6.8 In, the inoculation amount of described Lactobacillus salivarius strain is 0.5~1%, described PY medium is made up of the raw material of following weight components: unhydrolyzed macromolecular protein 50g, peptone 5g, tryptone 5g, yeast powder 10g, Anhydrous sodium acetate 20g, KH 2 PO 4 6g, MgSO 4 ∙7H 2 O 0.6g, MnSO 4 ∙4H 2 O 0.2g, water 1000g;

(2)于37℃进行发酵培养36-48h,培养完成后,收获菌体,即可。(2) Fermentation culture is carried out at 37°C for 36-48 hours. After the culture is completed, the cells are harvested.

实施例2 一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,包括以下步骤:Embodiment 2 A method for realizing high-density fermentation of lactic acid bacteria by using unshaped solid attachments, comprising the following steps:

(1)选择长势旺盛,并且保证接种后能够在4-8h达到完成对数生长期的优良发酵乳杆菌菌种进行活化,将活化后的发酵乳杆菌菌种接种于pH为6.8的PY培养基中,所述发酵乳杆菌菌种的接种量为0.5~1%,所述PY培养基由以下重量组分的原料组成:未水解大分子蛋白质50g,蛋白胨5g,胰蛋白胨5g,酵母粉10g,无水乙酸钠20g,KH2PO4 6g,MgSO4∙7H2O0.6g,MnSO4∙4H2O 0.2g,水1000 g;(1) Select the excellent Lactobacillus fermentum strains that grow vigorously and ensure that they can reach the logarithmic growth phase within 4-8 hours after inoculation for activation, and inoculate the activated Lactobacillus fermentum strains in PY medium with a pH of 6.8 Among them, the inoculum of the described Lactobacillus fermentum strain is 0.5~1%, and the PY medium is composed of the raw materials of the following weight components: unhydrolyzed macromolecular protein 50g, peptone 5g, tryptone 5g, yeast powder 10g, Anhydrous sodium acetate 20g, KH 2 PO 4 6g, MgSO 4 ∙7H 2 O 0.6g, MnSO 4 ∙4H 2 O 0.2g, water 1000g;

(2)于37℃进行发酵培养36-48h,培养完成后,收获菌体,即可。(2) Fermentation culture is carried out at 37°C for 36-48 hours. After the culture is completed, the cells are harvested.

实施例3 一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,包括以下步骤:Embodiment 3 A method for realizing high-density fermentation of lactic acid bacteria by using unshaped solid attachments, comprising the following steps:

(1)选择长势旺盛,并且保证接种后能够在4-8h达到完成对数生长期的优良乳酸片球菌菌种进行活化,将活化后的乳酸片球菌菌种接种于pH为6.8的PY培养基中,所述乳酸片球菌菌种的接种量为0.5~1%,所述PY培养基由以下重量组分的原料组成:未水解大分子蛋白质50g,蛋白胨5g,胰蛋白胨5g,酵母粉10g,无水乙酸钠20g,KH2PO4 6g,MgSO4∙7H2O0.6g,MnSO4∙4H2O 0.2g,水1000 g;(1) Select the excellent Pediococcus lactis strains that grow vigorously and ensure that they can reach the logarithmic growth phase within 4-8 hours after inoculation for activation, and inoculate the activated Pediococcus lactis strains in PY medium with a pH of 6.8 In, the inoculation amount of described Pediococcus lactis strain is 0.5~1%, and described PY medium is made up of the raw material of following weight components: unhydrolyzed macromolecular protein 50g, peptone 5g, tryptone 5g, yeast powder 10g, Anhydrous sodium acetate 20g, KH 2 PO 4 6g, MgSO 4 ∙7H 2 O 0.6g, MnSO 4 ∙4H 2 O 0.2g, water 1000g;

(2)于37℃进行发酵培养36-48h,培养完成后,收获菌体,即可。(2) Fermentation culture is carried out at 37°C for 36-48 hours. After the culture is completed, the cells are harvested.

试验例 本发明一种采用不定型固体附着物实现乳酸菌高密度发酵的方法的试验研究:Test Example The present invention is a kind of experimental research on the method for realizing high-density fermentation of lactic acid bacteria by using unshaped solid attachments:

1. 试验对象1. Test subjects

实验组:以本发明添加了未水解蛋白质的培养基的发酵方法,分别对唾液乳杆菌、发酵乳杆菌和乳酸片球菌进行高密度培养。Experimental group: Lactobacillus salivarius, Lactobacillus fermentum and Pediococcus lactis were respectively cultured at high density with the fermentation method of the present invention adding the unhydrolyzed protein culture medium.

对照组:以不添加未水解蛋白质的基础培养基的发酵方法,分别对唾液乳杆菌、发酵乳杆菌和乳酸片球菌进行高密度培养。Control group: Lactobacillus salivarius, Lactobacillus fermentum and Pediococcus lactis were cultured at high density by the fermentation method of basal medium without adding unhydrolyzed protein.

2. 试验方法2. Test method

2.1菌落总数的测量2.1 Measurement of the total number of colonies

菌落总数的测定采用平板计数法。取1 mL样品用无菌水10倍梯度稀释后,再吸取200 μL倾入培养皿中,接着倒入温度不超过70℃的MRS琼脂培养基。经37℃培养48 h后,对肉眼可见的菌落进行计数。菌落数要求在30~300个为有效稀释梯度,根据稀释的倍数,计算出原样品中的菌落数。由图1-3可知,基础培养基(对照组)培养结束后(24 h)菌落总数为108-9 cfu/mL,而本发明方法(实验组)发酵结束可以获得菌落总数为1010-12cfu/mL,相当于对照组的100~1000倍。The total number of colonies was determined by plate count method. Take 1 mL of sample diluted 10-fold with sterile water, then pipette 200 μL into a petri dish, and then pour it into MRS agar medium with a temperature not exceeding 70 °C. After 48 h incubation at 37°C, the colonies visible to the naked eye were counted. The number of colonies is required to be between 30 and 300 as an effective dilution gradient, and the number of colonies in the original sample is calculated according to the dilution multiple. It can be seen from Figure 1-3 that after the basal medium (control group) is cultured (24 h), the total number of colonies is 10 8-9 cfu/mL, while the total number of colonies obtained by the method of the present invention (experimental group) after fermentation is 10 10- 12 cfu/mL, equivalent to 100-1000 times that of the control group.

2.2耐高温实验2.2 High temperature resistance test

无菌条件下分别取培养12 h的对照组和实验组的乳酸菌菌液,转移1mL至无菌离心管中,在50℃、60℃、70℃水浴30 min后,冰水迅速冷却至常温,然后测定初始及高温水浴后的菌落总数。根据菌体存活率,判断不同处理组乳酸菌的耐高温能力。由图4-6可知,本发明方法培养乳酸菌时,菌体耐高温能力显著增强,特别是60℃时处理30 min,对照组的乳酸菌全部死亡,而实验组均有不同程度的存活率。但是50℃处理时,对照组的菌体存活率为73~86%,实验组的存活率为85~95%。而70℃处理30min,所有的菌体全部死亡,存活率为0。Take the lactic acid bacteria liquids of the control group and the experimental group that have been cultured for 12 h under aseptic conditions, transfer 1 mL to a sterile centrifuge tube, and after 30 min in a water bath at 50 °C, 60 °C, and 70 °C, the ice water is rapidly cooled to room temperature. The total number of colonies was then determined initially and after the high temperature water bath. According to the bacterial survival rate, the high temperature resistance ability of lactic acid bacteria in different treatment groups was judged. As can be seen from Figures 4-6, when the lactic acid bacteria are cultivated by the method of the present invention, the high temperature resistance of the bacteria body is significantly enhanced, especially when treated at 60°C for 30 min, all the lactic acid bacteria in the control group died, while the experimental groups had varying degrees of survival. However, when treated at 50 °C, the survival rate of the control group was 73-86%, and the survival rate of the experimental group was 85-95%. However, when treated at 70°C for 30 min, all the cells died and the survival rate was 0.

2.3模拟胃液及胆盐配制及实验方法2.3 Preparation and experimental methods of simulated gastric juice and bile salts

模拟胃液参照JJ Ahire等(2011)的配方:蛋白胨8.3,葡萄糖3.5,NaCL2.05,KH2PO4 0.6, CaCl2 0.11, KCL 0.37,胆盐0.05,溶菌酶0.1,胃蛋白酶13.3(单位:mg/mL),最终pH值用1mol/L的HCL调节到2.50。使用时稀释10倍。The simulated gastric juice refers to the formula of JJ Ahire et al. (2011): peptone 8.3, glucose 3.5, NaCL 2.05, KH 2 PO 4 0.6, CaCl 2 0.11, KCL 0.37, bile salt 0.05, lysozyme 0.1, pepsin 13.3 (unit: mg /mL), and the final pH was adjusted to 2.50 with 1 mol/L HCL. Dilute 10 times when using.

测定菌体在模拟胃液中的存活率时,取乳酸菌菌液10000 g离心5 min,弃去上清液后,换成等量的模拟胃液(10倍稀释),37℃培养30-180 min后,测量菌落总数。图7-9表明,实验组与对照组的乳酸菌对模拟胃酸均有一定的耐受能力,随着处理时间的延长,菌体存活率迅速下降。而实验组的存活率要显著高于对照组(P < 0.05)。When measuring the survival rate of bacteria in simulated gastric juice, centrifuge the lactic acid bacteria liquid at 10,000 g for 5 min, discard the supernatant, replace it with the same amount of simulated gastric juice (10-fold dilution), and incubate at 37°C for 30-180 min. , to measure the total number of colonies. Figures 7-9 show that the lactic acid bacteria in the experimental group and the control group have a certain tolerance to simulated gastric acid. The survival rate of the experimental group was significantly higher than that of the control group (P < 0.05).

胆盐的配制是按照0.5-2%的质量分数,配制相应的胆盐溶液即可。图10-12表明,受试乳酸菌对于胆盐均表现出较强的耐受力。随着胆盐浓度的上升,菌体存活率有所下降。总体来说,实验组菌体存活率显著高于对照组(P < 0.05)。The preparation of bile salts is to prepare a corresponding bile salt solution according to the mass fraction of 0.5-2%. Figures 10-12 show that the tested lactic acid bacteria showed strong tolerance to bile salts. With the increase of bile salt concentration, the bacterial survival rate decreased. Overall, the bacterial survival rate in the experimental group was significantly higher than that in the control group (P < 0.05).

对于本领域技术人员而言,显然本发明不限于上述示范性实施例的细节,而且在不背离本发明的精神或基本特征的情况下,能够以其他的具体形式实现本发明。因此,无论从哪一点来看,均应将实施例看作是示范性的,而且是非限制性的,本发明的范围由所附权利要求而不是上述说明限定,因此旨在将落在权利要求的等同要件的含义和范围内的所有变化囊括在本发明内。不应将权利要求中的任何附图标记视为限制所涉及的权利要求。It will be apparent to those skilled in the art that the present invention is not limited to the details of the above-described exemplary embodiments, but that the present invention may be embodied in other specific forms without departing from the spirit or essential characteristics of the invention. Therefore, the embodiments are to be regarded in all respects as illustrative and not restrictive, and the scope of the invention is to be defined by the appended claims rather than the foregoing description, which are therefore intended to fall within the scope of the claims. All changes within the meaning and scope of the equivalents of , are included in the present invention. Any reference signs in the claims shall not be construed as limiting the involved claim.

Claims (5)

1.一种采用不定型固体附着物实现乳酸菌高密度发酵的方法,其特征在于,包括以下步骤:1. a kind of method that adopts amorphous solid attachment to realize lactic acid bacteria high density fermentation, is characterized in that, comprises the following steps: (1)选择长势旺盛,并且保证接种后能够在4-8h达到完成对数生长期的优良乳酸菌菌种进行活化,将活化后的乳酸菌菌种接种于乳酸菌培养基中;(1) Select the excellent lactic acid bacteria strains that grow vigorously and ensure that they can reach the logarithmic growth phase within 4-8 hours after inoculation for activation, and inoculate the activated lactic acid bacteria strains in the lactic acid bacteria medium; (2)于37℃进行发酵培养,培养完成后,收获菌体,即可;(2) Fermentation culture is carried out at 37°C, and after the culture is completed, the cells are harvested; 其中,乳酸菌培养基为PY培养基;Wherein, the lactic acid bacteria culture medium is PY culture medium; 所述PY培养基由以下重量组分的原料组成:未水解大分子蛋白质50g,蛋白胨5g,胰蛋白胨5g,酵母粉10g,无水乙酸钠20g,KH2PO4 6g,MgSO4∙7H2O 0.6g,MnSO4∙4H2O 0.2g,水1000g。The PY medium is composed of the following raw materials by weight: 50 g of unhydrolyzed macromolecular protein, 5 g of peptone, 5 g of tryptone, 10 g of yeast powder, 20 g of anhydrous sodium acetate, 6 g of KH 2 PO 4 , MgSO 4 ∙7H 2 O 0.6g, MnSO 4 ∙4H 2 O 0.2g, water 1000g. 2.根据权利要求1所述的方法,其特征在于,步骤(1)所述乳酸菌菌种是唾液乳杆菌、发酵乳杆菌和乳酸片球菌中的一种。2 . The method according to claim 1 , wherein the lactic acid bacteria strain in step (1) is one of Lactobacillus salivarius, Lactobacillus fermentum and Pediococcus lactis. 3 . 3.根据权利要求1所述的方法,其特征在于,步骤(1)所述乳酸菌菌种的接种量为0.5~1%。3 . The method according to claim 1 , wherein the inoculation amount of the lactic acid bacteria strain in step (1) is 0.5-1%. 4 . 4.根据权利要求1所述的方法,其特征在于,所述PY培养基的pH为6.8。4. The method according to claim 1, wherein the pH of the PY medium is 6.8. 5.根据权利要求1所述的方法,其特征在于,步骤(2)所述发酵的时间为36-48h。5 . The method according to claim 1 , wherein the fermentation time of step (2) is 36-48 h. 6 .
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Publication number Priority date Publication date Assignee Title
CN101338283A (en) * 2007-07-06 2009-01-07 内蒙古农业大学 A kind of Lactobacillus casei and its application in solid-state fermentation
CN102057046A (en) * 2008-04-09 2011-05-11 钴技术有限公司 Immobilized product tolerant microorganisms
CN103013893A (en) * 2013-01-21 2013-04-03 黑龙江八一农垦大学 Lactobacillus plantarum CCL67 and application of same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101338283A (en) * 2007-07-06 2009-01-07 内蒙古农业大学 A kind of Lactobacillus casei and its application in solid-state fermentation
CN102057046A (en) * 2008-04-09 2011-05-11 钴技术有限公司 Immobilized product tolerant microorganisms
CN103013893A (en) * 2013-01-21 2013-04-03 黑龙江八一农垦大学 Lactobacillus plantarum CCL67 and application of same

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