CN105002126B - A kind of simple batch culture process of facultative aerobe - Google Patents
A kind of simple batch culture process of facultative aerobe Download PDFInfo
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Abstract
本发明公开了一种需氧菌或兼性需氧菌的简易批量培养方法,采用密封箱体多层方盘固体平面发酵装置培养。所述的密封箱体和方盘是以不易变形的耐热薄板材质制作,密封箱体的大小以仅能容纳指定数量层叠放置的方盘为准,密封盖的对角处分别设置有2个接种孔。采用一次性注入培养基、一次性灭菌、一次性形成多层培养表面、一次性接种、一次性洗涤收获。其设备简单、成本低廉、操作方便、不易污染、生产效率高,与传统发酵罐液体发酵培养方法相比,其培养效率可提高50倍以上,细菌浓度可高达1500~2000亿个/ml,降低生产成本50%以上,解决了在需氧菌或兼性需氧菌的批量生产制备过程中普遍存在生产效率低、菌液浓缩困难、污水排放多或生产成本高等瓶颈问题。
The invention discloses a simple batch culture method for aerobic bacteria or facultative aerobic bacteria, which is cultivated by a multi-layer square plate solid plane fermentation device with a sealed box. The sealed box and the square plate are made of heat-resistant sheet material that is not easy to deform. The size of the sealed box is based on the size that can only accommodate a specified number of stacked square plates. There are two opposite corners of the sealed cover. Inoculation hole. It adopts one-time injection of culture medium, one-time sterilization, one-time formation of multi-layer culture surface, one-time inoculation, one-time washing and harvesting. Its equipment is simple, low in cost, easy to operate, not easy to pollute, and high in production efficiency. Compared with the traditional fermenter liquid fermentation culture method, its culture efficiency can be increased by more than 50 times, and the bacterial concentration can be as high as 150-200 billion/ml, reducing The production cost is more than 50%, which solves the common bottleneck problems such as low production efficiency, difficult concentration of bacterial solution, excessive sewage discharge or high production cost in the mass production and preparation of aerobic bacteria or facultative aerobic bacteria.
Description
技术领域technical field
本发明属于微生物发酵领域,具体涉及一种兼性需氧菌的简易批量培养方法。The invention belongs to the field of microbial fermentation, and in particular relates to a simple batch culture method for facultative aerobic bacteria.
背景技术Background technique
发酵是指人们借助微生物在有氧或无氧条件下的生命活动来制备微生物菌体本身、或者直接代谢产物或次级代谢产物的过程(邱立友,王明道主编 .微生物学 :化学工业出版社 ,2012 :343 )。随着生物技术的不断发展,在微生物发酵领域对兼性需氧菌的纯培养需求日益增多,目前,兼性需氧菌的实验室培养是一种常见、简单、成熟技术,如液体、固体培养;试管、平皿、茄形瓶培养等,但大批量生产制备,其工艺难度较大。在大批量兼性需氧菌的纯培养发酵领域,多采用传统的发酵罐液体通气培养方法,该方法普遍存在生产环节易污染、生产效率较低、菌液浓缩困难、污水排放多及生产成本高等瓶颈。Fermentation refers to the process in which people use the life activities of microorganisms under aerobic or anaerobic conditions to prepare microbial cells themselves, or direct metabolites or secondary metabolites (Qiu Liyou, Wang Mingdao editor-in-chief. Microbiology: Chemical Industry Press, 2012: 343). With the continuous development of biotechnology, the demand for pure culture of facultative aerobic bacteria in the field of microbial fermentation is increasing. At present, laboratory culture of facultative aerobic bacteria is a common, simple and mature technology, such as liquid, solid Cultivation; test tube, plate, eggplant-shaped bottle culture, etc., but the preparation of mass production is difficult. In the field of pure culture and fermentation of large quantities of facultative aerobic bacteria, traditional fermentation tank liquid aeration culture methods are mostly used. This method generally has the disadvantages of easy pollution in the production process, low production efficiency, difficulty in concentrating the bacterial liquid, excessive sewage discharge and production costs. Advanced bottleneck.
密封箱体多层固体发酵培养方法,其设备简单、成本低廉、操作方便、不易污染、生产效率高;该技术的应用可显著降低培养基的用量,节约产品浓缩成本,降低能耗,减少污水排放。与传统发酵罐液体发酵培养方法相比,其培养效率可提高50倍以上,细菌浓度可高达1500 ~2000亿个/ml,降低生产成本50%以上。The multi-layer solid fermentation culture method in a sealed box has simple equipment, low cost, convenient operation, no pollution, and high production efficiency; the application of this technology can significantly reduce the amount of medium used, save product concentration costs, reduce energy consumption, and reduce sewage emission. Compared with the traditional fermenter liquid fermentation culture method, the culture efficiency can be increased by more than 50 times, the bacterial concentration can be as high as 150-200 billion/ml, and the production cost can be reduced by more than 50%.
经百度搜索引擎、维普中文科技期刊数据库等搜索“固体平面发酵”、“固体平面培养”、“多层方盘发酵培养”等词汇,均未查阅到相同或相近的内容。现行的微生物固体发酵培养,是在本领域广泛应用的传统技术、方法,其工艺特征在于混菌发酵培养,即微生物与固体培养基颗粒混合在一起。本专利技术提供的密封箱体多层固体培养方法,工艺特征是浓缩纯培养,即单一细菌的纯化培养。细菌的批量纯化培养在许多生物技术领域如菌种生产、疫苗生产、微生态制剂和生物酶制剂生产等都有着广泛的技术需求。After searching words such as "solid plane fermentation", "solid plane culture" and "multi-layer square plate fermentation culture" through Baidu search engine and VIP Chinese science and technology journal database, no identical or similar content was found. The current microbial solid fermentation culture is a traditional technology and method widely used in this field. Its process is characterized by mixed bacteria fermentation culture, that is, microorganisms and solid medium particles are mixed together. The multi-layer solid culture method in a sealed box provided by this patent technology is characterized by concentrated pure culture, that is, the purified culture of a single bacterium. The batch purification and cultivation of bacteria has a wide range of technical requirements in many biotechnology fields such as strain production, vaccine production, probiotics and biological enzyme production.
发明内容Contents of the invention
本发明的目的在于针对在兼性需氧菌的批量生产制备过程中普遍存在生产效率低、菌液浓缩困难、污水排放多或生产成本高等瓶颈问题,提供一种兼性需氧菌的简易批量培养方法,该培养方法设备简单、成本低廉、操作方便、不易污染、生产效率高,与传统发酵罐液体发酵培养方法相比,其培养效率可提高50倍以上,细菌浓度可高达1500~2000亿个/ml,降低生产成本50%以上。The purpose of the present invention is to provide a simple batch method for facultative aerobic bacteria in view of the common bottleneck problems such as low production efficiency, difficulty in concentrating bacterial solution, excessive sewage discharge or high production cost in the batch production and preparation process of facultative aerobic bacteria. The cultivation method has simple equipment, low cost, convenient operation, no pollution, and high production efficiency. Compared with the traditional fermentation tank liquid fermentation cultivation method, the cultivation efficiency can be increased by more than 50 times, and the bacterial concentration can be as high as 150 to 200 billion pcs/ml, reducing the production cost by more than 50%.
为实现上述发明目的,本发明采用如下技术方案:In order to realize the above-mentioned purpose of the invention, the present invention adopts following technical scheme:
一种兼性需氧菌的简易批量培养方法,采用密封箱体多层方盘固体平面发酵装置培养;所述的密封箱体和方盘是以不易变形的耐热薄板材质制作,方盘的数量为10~20个,密封箱体的大小以仅能容纳指定数量层叠放置的方盘为准,密封盖的对角处分别设置2个直径为22mm的接种孔,接种孔用硅胶塞密封;所述密封箱体开口处设有封闭开口的密封盖,所述密封盖与箱体开口边缘之间设有密封胶垫,所述密封盖、密封胶垫及箱体经贯穿三者的锁闭螺丝固定连接;锁闭螺丝设置于密封盖四角。A simple batch culture method for facultative aerobic bacteria, which adopts a sealed box multi-layer square plate solid plane fermentation device for cultivation; the sealed box and square plate are made of heat-resistant thin plate material that is not easily deformed, and the square plate The quantity is 10~20, the size of the sealed box is subject to the specified number of stacked square plates, and two inoculation holes with a diameter of 22mm are set at the opposite corners of the sealing cover, and the inoculation holes are sealed with silicone plugs; The opening of the sealed box body is provided with a sealing cover for closing the opening, and a sealing rubber pad is provided between the sealing cover and the opening edge of the box body, and the sealing cover, the sealing rubber pad and the box body are locked through the three. The connection is fixed by screws; the locking screws are set at the four corners of the sealing cover.
所述的不易变形的耐热薄板材质是不锈钢。The material of the non-deformable heat-resistant thin plate is stainless steel.
每个方盘的尺寸根据生产需求进行设定,如根据生产需求设置为:长45㎝~60㎝;宽30㎝~45㎝;高1.5㎝~2.5㎝。The size of each square plate is set according to production requirements, such as: length 45cm~60cm; width 30cm~45cm; height 1.5cm~2.5cm.
所述的兼性需氧菌的简易批量培养方法,包括以下步骤:The simple batch culture method of described facultative aerobic bacteria comprises the following steps:
1)通过密封盖上预留的接种孔,注入按方盘内表面积计算能形成厚度为3mm~5mm凝胶的琼脂培养基混悬液,用硅胶塞密封接种孔,置高温灭菌设备中常规灭菌,待箱体温度降至50℃~60℃,震荡箱体混匀培养基,以方盘位置为基准竖立箱体,静置片刻使琼胶从缝隙中流入方盘,待琼胶液面平衡稳定,然后快速水平放置箱体并使方盘开口朝上,使融化的琼脂均匀分布于每个方盘中;1) Through the inoculation hole reserved on the sealing cover, inject the agar medium suspension that can form a gel with a thickness of 3mm~5mm according to the inner surface area of the square plate, seal the inoculation hole with a silica gel plug, and place it in a high-temperature sterilization equipment for routine use. Sterilize, wait for the temperature of the box to drop to 50°C~60°C, shake the box to mix the culture medium, erect the box based on the position of the square plate, let the agar flow into the square plate from the gap for a while, and wait for the agar solution The surface is balanced and stable, then quickly place the box horizontally and make the opening of the square plate face up, so that the melted agar is evenly distributed in each square plate;
2)待琼脂降温凝固,按箱体容积的1%~2%接种液体菌种,接种采取无菌术式,借助超净工作台或火焰封闭将菌种注入或滴入接种孔中,菌种浓度保持5亿个/ml以上,接种后以方盘位置为基准竖立箱体,静置片刻使菌液从缝隙中流入方盘,待菌种液面平衡稳定,然后快速水平放置箱体并使方盘开口朝上,轻轻倾斜、往返震荡箱体,使菌种充分涂布于琼脂培养基表面,置适温条件下培养24 h~72 h形成菌苔;2) After the agar cools down and solidifies, inoculate the liquid strains according to 1%~2% of the volume of the box. The inoculation adopts an aseptic method, and injects or drops the strains into the inoculation hole with the help of an ultra-clean workbench or flame closure. Keep the concentration above 500 million/ml. After inoculation, erect the box with the position of the square plate as the reference, let the bacteria liquid flow into the square plate from the gap for a while, wait for the liquid level of the bacteria to be balanced and stable, then quickly place the box horizontally and make it With the opening of the square plate facing upwards, gently tilt the box and vibrate the box back and forth, so that the bacteria are fully coated on the surface of the agar medium, and cultured at a suitable temperature for 24 h to 72 h to form a bacterial lawn;
3)培养物收获时按箱体容积的15%~20%注入冲洗液,震荡箱体充分洗涤菌苔后倾斜箱体,通过接种孔导出洗涤液即获得浓缩纯培养菌液。3) When the culture is harvested, 15%~20% of the box volume is injected with washing liquid, the box is shaken to fully wash the bacterial lawn, and then the box is tilted, and the washing liquid is exported through the inoculation hole to obtain concentrated pure culture liquid.
所述的兼性需氧菌的简易批量培养方法,细菌在多层方盘固体培养基上发酵培养,采用一次性注入培养基、一次性灭菌、一次性形成多层培养表面、一次性接种、一次性洗涤收获。In the simple batch culture method of facultative aerobic bacteria, the bacteria are fermented and cultivated on a multi-layer square plate solid medium, and the culture medium is injected into the culture medium in one time, sterilized in one time, a multi-layer culture surface is formed in one time, and inoculated in one time. , One-time washing harvest.
为防止产品污染,通过无菌操作采用注射针头、胶管连接和过滤空气箱体内增压的方法,将浓缩菌液导入容器中,获得无污染的浓缩纯培养菌液。In order to prevent product contamination, through aseptic operation, the method of injecting needles, rubber hose connections and pressurization in the filtered air box is used to introduce the concentrated bacterial liquid into the container to obtain a non-polluting concentrated pure culture bacterial liquid.
箱体中残留的培养基,通过加热或高温灭菌后,在培养基降温凝固前通过接种孔倒出,注水冲洗,将接种孔倒置、淋干备用。The medium remaining in the box is sterilized by heating or high temperature, poured out through the inoculation hole before the medium cools down and solidifies, rinses with water, turns the inoculation hole upside down, and dries for later use.
本发明是将实验室中细菌的琼脂平板培养方法进行有效放大。在实验室常用的平皿或茄形瓶琼脂平板培养细菌的方法,因其有效培养面积较小,仅应用于小批量细菌培养,不适用于细菌的大量生产制备。1个密封箱体多层方盘的有效培养面积约为30000 cm2,相当于200个规格为500ml茄形瓶的培养面积或468个直径为9 cm平皿的培养面积。密封箱体多层方盘培养技术在大批量兼性需氧菌生产制备中具有显著的应用优势。The invention effectively amplifies the agar plate culture method of bacteria in the laboratory. The method of cultivating bacteria on the agar plate of the plate or eggplant-shaped bottle commonly used in the laboratory is only applicable to small batches of bacterial culture because of its small effective culture area, and is not suitable for the mass production and preparation of bacteria. The effective culture area of a multi-layer square plate with a sealed box is about 30000 cm 2 , which is equivalent to the culture area of 200 eggplant-shaped bottles with a specification of 500ml or the culture area of 468 plates with a diameter of 9 cm. The multi-layer square plate culture technology in a sealed box has significant application advantages in the production and preparation of large quantities of facultative aerobic bacteria.
本发明的有益效果在于:本发明的设备简单、成本低廉、操作方便、不易污染、生产效率高,与传统发酵罐液体发酵培养方法相比,其培养效率可提高50倍以上,细菌浓度可高达1500~2000亿个/ml,降低生产成本50%以上;解决了在兼性需氧菌的批量生产制备过程中普遍存在生产效率低、菌液浓缩困难、污水排放多或生产成本高等瓶颈问题。The beneficial effects of the present invention are: the equipment of the present invention is simple, low in cost, easy to operate, not easy to pollute, and high in production efficiency. Compared with the traditional fermenter liquid fermentation culture method, its culture efficiency can be increased by more than 50 times, and the bacterial concentration can be as high as 150-200 billion/ml, reducing the production cost by more than 50%; solving the common bottleneck problems in the mass production and preparation of facultative aerobic bacteria, such as low production efficiency, difficult concentration of bacterial liquid, excessive sewage discharge or high production cost.
附图说明Description of drawings
图1为方盘的结构示意图;Fig. 1 is the structural representation of square plate;
图2为密封培养箱部分分解结构示意图;Fig. 2 is a schematic diagram of a partially decomposed structure of a sealed incubator;
图3为密封培养箱整体结构分解结构示意图;Fig. 3 is a schematic diagram of the decomposition structure of the overall structure of the sealed incubator;
图中,10—方盘,20—箱体,30—密封胶垫,40—密封盖,410—锁闭螺丝,50—接种孔。In the figure, 10—square plate, 20—box body, 30—sealing rubber pad, 40—sealing cover, 410—locking screw, 50—inoculation hole.
具体实施方式detailed description
本发明用下列实施例来进一步说明本发明,但本发明的保护范围并不限于下列实施例。The present invention further illustrates the present invention with following examples, but protection scope of the present invention is not limited to following examples.
福建某动物微生态制剂厂,曾应用液体发酵罐通气发酵方法生产大肠埃希氏菌C600,生产工艺较为复杂,离心浓缩过程中的人工劳动繁重,易受杂菌污染,生产效率低下。也曾改用茄形瓶营养琼脂平面培养,显著降低了原材料消耗,因其有效培养面积较小,人工劳动繁重,操作环节繁琐、污染机率高,生产效率受到限制。应用本发明的密封箱体多层方盘固体平面发酵培养技术,设备简单,投入少,生产工艺简化,产品污染机会减少,降低了生产成本,减少了污水排放,生产效率显著提高,连续生产液体微生态制剂成品200余吨,取得了良好的效益。An animal micro-ecological preparation factory in Fujian used a liquid fermenter aerated fermentation method to produce Escherichia coli C600. The production process is relatively complicated. The manual labor in the centrifugal concentration process is heavy, it is easily contaminated by bacteria, and the production efficiency is low. Also used eggplant-shaped bottle nutrient agar plane culture, which significantly reduced the consumption of raw materials, because of its small effective culture area, heavy manual labor, cumbersome operation links, high probability of pollution, and limited production efficiency. Applying the sealing box multi-layer square plate solid plane fermentation culture technology of the present invention, the equipment is simple, the investment is small, the production process is simplified, the chance of product pollution is reduced, the production cost is reduced, the sewage discharge is reduced, the production efficiency is significantly improved, and the continuous production of liquid There are more than 200 tons of finished microecological preparations, and good benefits have been achieved.
现以生产10 L浓度为1500亿个/ml的大肠埃希氏菌(C600)浓缩菌液为例,对上述三种培养方法进行比较如下:Taking the production of 10 L of Escherichia coli (C600) concentrated bacterial liquid with a concentration of 150 billion/ml as an example, the above three cultivation methods are compared as follows:
实施例1液体发酵罐通气培养发酵Embodiment 1 Liquid fermenter aerated culture fermentation
1)设备1) Equipment
500 L发酵罐;超净工作台(1400×690×520mm);大容量冷冻离心机(DL-4000B,500 ml×6)。500 L fermentation tank; ultra-clean bench (1400×690×520mm); large-capacity refrigerated centrifuge (DL-4000B, 500 ml×6).
2)培养基制备2) Culture medium preparation
普通肉汤培养基:蛋白胨5 kg、牛肉膏1.5 kg、氯化钠2.5 kg、蒸馏水500 L(牛肉膏、蛋白胨为北京奥博星生物公司生产)。Ordinary broth medium: peptone 5 kg, beef extract 1.5 kg, sodium chloride 2.5 kg, distilled water 500 L (beef extract and peptone were produced by Beijing Aoboxing Biological Company).
混匀培养基后,用10%氢氧化钠调节至pH7.4,发酵罐以121℃高压灭菌15 min,冷却备用(氯化钠为市售分析纯试剂)。After the medium was mixed, the pH was adjusted to 7.4 with 10% sodium hydroxide, and the fermenter was autoclaved at 121 °C for 15 min, and then cooled for later use (sodium chloride was a commercially available analytical reagent).
3)接种培养3) Inoculation and culture
通过无菌术式接入大肠埃希氏菌C600菌种100 ml,菌种浓度为5亿个/ml,发酵罐底部通入无菌超滤空气,打开发酵罐顶部的无菌超滤排气孔,37 ℃通气培养36 h,细菌浓度达到30亿个/ml。Insert 100 ml of Escherichia coli C600 strain through aseptic technique, the strain concentration is 500 million/ml, pass sterile ultra-filtered air into the bottom of the fermenter, and open the sterile ultra-filter exhaust on the top of the fermenter Wells were incubated at 37°C for 36 h with aeration, and the bacterial concentration reached 3 billion/ml.
4)菌液浓缩4) Bacterial liquid concentration
细菌培养液的分装在超净工作台上进行,将培养菌液分别、多次导出至塑料离心瓶中,离心机每次离心容量为3000 ml(500 ml×6),密封离心瓶后,分别置于离心杯中、对角离心杯平衡。4000 rpm离心沉淀10 min弃上清,取60 ml灭菌生理盐水依次洗涤6个离心瓶中的沉淀物,获得约60 ml浓度为1500亿个/ml的浓缩菌液。500 L发酵培养菌液,共累计离心167次,收集洗涤液,获得约10 L浓度为1500亿个/ml的浓缩菌液。The subpackage of the bacterial culture solution is carried out on the ultra-clean workbench, and the culture solution is exported to plastic centrifuge bottles several times. The centrifuge capacity is 3000 ml (500 ml×6) each time. After sealing the centrifuge bottle, Place them in a centrifugal cup and balance them in a diagonal centrifugal cup. Centrifuge at 4000 rpm for 10 min, discard the supernatant, take 60 ml of sterilized normal saline to wash the sediment in 6 centrifuge bottles in turn, and obtain about 60 ml of concentrated bacterial solution with a concentration of 150 billion cells/ml. 500 L of fermentation culture liquid was centrifuged for a total of 167 times, and the washing liquid was collected to obtain about 10 L of concentrated bacterial liquid with a concentration of 150 billion cells/ml.
5)主要设备投资、生产成本5) Major equipment investment and production cost
设备:10.2万元(发酵罐4.8万元;超净工作台1.2万元;大容量冷冻离Equipment: 102,000 yuan (fermentation tank 48,000 yuan; ultra-clean workbench 12,000 yuan; large-capacity freezer
心机4.2万)。scheming 42,000).
培养基:1480元(蛋白胨5 kg×200元;牛肉膏1.5 kg×300元;氯化钠Medium: 1480 yuan (peptone 5 kg×200 yuan; beef extract 1.5 kg×300 yuan; sodium chloride
2.5 kg×12元)。2.5 kg x 12 yuan).
水电费:591元(灭菌15 KV×3 h×1元;培养1 KV×36/2 h×1元;Water and electricity fee: 591 yuan (sterilization 15 KV×3 h×1 yuan; culture 1 KV×36/2 h×1 yuan;
离心1 KV×167/6 h×1元;蒸馏水500 L×1元)。Centrifuge 1 KV×167/6 h×1 yuan; distilled water 500 L×1 yuan).
人员工资:800元(2人×2 d×200元)。Staff salary: 800 yuan (2 people x 2 d x 200 yuan).
6)废物排放6) Waste discharge
废弃培养基500 L;器具洗刷用水200 L。500 L of discarded culture medium; 200 L of water for washing equipment.
实施例2 茄形瓶营养琼脂平面培养Embodiment 2 Nutrient agar plane culture in eggplant-shaped bottle
1) 设备器材1) Equipment and equipment
卧式矩形压力蒸汽灭菌器(规格:30L,1018×500×600mm);恒温培养箱(规格:610×530×1360 mm);超净工作台(规格:1400×690×520mm);大容量振荡器;茄形瓶(规格:500ml)。Horizontal rectangular pressure steam sterilizer (specification: 30L, 1018×500×600mm); constant temperature incubator (specification: 610×530×1360 mm); ultra-clean workbench (specification: 1400×690×520mm); large capacity Shaker; eggplant-shaped bottle (specification: 500ml).
2)培养基制备2) Culture medium preparation
营养琼脂培养基:蛋白胨0.1 kg;牛肉膏0.03 kg;氯化钠0.05 kg;琼脂0.15 kg;蒸馏水10 L。Nutrient agar medium: peptone 0.1 kg; beef extract 0.03 kg; sodium chloride 0.05 kg; agar 0.15 kg; distilled water 10 L.
混匀培养基,用10%氢氧化钠调节至pH7.4,分装至200个茄形瓶中,每瓶50 ml,用硅胶塞密封瓶口,置121 ℃高压灭菌15 min,待温度降至50℃~60℃,震荡茄形瓶混匀培养基,水平放置,待琼脂降温凝固,形成厚度为3mm~5mm营养琼脂凝胶备用。Mix the culture medium, adjust to pH 7.4 with 10% sodium hydroxide, distribute to 200 eggplant-shaped bottles, 50 ml per bottle, seal the bottle mouth with a silica gel stopper, place at 121 ℃ for 15 min, and wait for temperature Lower the temperature to 50°C~60°C, shake the eggplant-shaped bottle to mix the medium, place it horizontally, wait for the agar to cool down and solidify, and form a nutrient agar gel with a thickness of 3mm~5mm for later use.
3) 接种培养3) Inoculation culture
借助超净工作台,通过无菌术式,每个茄形瓶接入大肠埃希氏菌C600菌种3 ml,菌种浓度为5亿个/ml,硅胶塞密封瓶口。倾斜、摇动茄形瓶,使菌种充分涂布于琼脂培养基表面,置37 ℃培养36 h, 待菌种生长形成菌苔。With the help of an ultra-clean workbench, through aseptic procedures, 3 ml of Escherichia coli C600 strains were inserted into each eggplant-shaped bottle, with a strain concentration of 500 million/ml, and a silicone plug sealed the mouth of the bottle. Tilt and shake the eggplant-shaped bottle so that the bacteria are fully coated on the surface of the agar medium, and cultured at 37 °C for 36 h, until the bacteria grow and form a lawn.
4)菌液收集4) Bacterial liquid collection
通过无菌术式每个茄形瓶注入灭菌生理盐水50ml,密封瓶口后将茄形瓶稳定于振荡机上,50次/min震荡15 min,充分洗涤菌苔,导出洗涤液至无菌容器,获得约10 L浓度为1500亿个/ml的浓缩菌液。Inject 50ml of sterilized physiological saline into each eggplant-shaped bottle through aseptic technique, seal the bottle mouth, stabilize the eggplant-shaped bottle on the shaker, shake at 50 times/min for 15 minutes, fully wash the bacterial lawn, and export the washing liquid to a sterile container , to obtain about 10 L of concentrated bacterial liquid with a concentration of 150 billion cells/ml.
5)主要设备投资、生产成本5) Major equipment investment and production cost
设备器材:6.7万元(蒸汽灭菌器2.8万元;恒温培养箱2万元;超净工作台1.2万元;大容量振荡器0.3万元;茄形瓶200×20元)Equipment and equipment: 67,000 yuan (28,000 yuan for steam sterilizer; 20,000 yuan for constant temperature incubator; 12,000 yuan for ultra-clean workbench; 3,000 yuan for large-capacity oscillator; 200×20 yuan for eggplant-shaped bottles)
培养基:44.6元(蛋白胨0.1 kg×200元;牛肉膏0.03 kg×300元;氯化Medium: 44.6 yuan (peptone 0.1 kg×200 yuan; beef extract 0.03 kg×300 yuan; chlorinated
钠0.05 kg×12元;琼脂0.15 kg×100元)。Sodium 0.05 kg×12 yuan; agar 0.15 kg×100 yuan).
水电费:103元(灭菌5 KV×3 h×5次×1元;培养1 KV×36/2 h×1元;Water and electricity fee: 103 yuan (sterilization 5 KV×3 h×5 times×1 yuan; culture 1 KV×36/2 h×1 yuan;
蒸馏水10 L×1元;器材洗刷用自来水1000 L)。10 L of distilled water × 1 yuan; 1000 L of tap water for washing equipment).
人员工资:1200元(2人×3 d×200元)。Staff salary: 1200 yuan (2 people x 3 d x 200 yuan).
6)废物排放6) Waste discharge
废弃培养基10 L;器具洗刷用水1000 L。10 L of discarded culture medium; 1000 L of water for washing equipment.
实施例3 密封箱体多层方盘固体平面培养Example 3 Culture on Solid Plane with Multi-layer Square Plate in Sealed Box
1) 设备1) Equipment
卧式矩形压力蒸汽灭菌器(规格:30L,1018×500×600 mm);恒温培养箱(规格:750×600×600 mm);超净工作台(规格:1400×690×520 mm);大容量振荡器;不锈钢密封箱体多层方盘,包括:不锈钢方盘12个,长宽高60×45×2.0㎝;不锈钢密封箱体1个,长宽高60×45×24㎝;密封盖1个,长宽49×28㎝,密封盖表面对角处分别设置2个可用硅胶塞密封的接种孔操作,借助硅胶垫将密封盖和箱体连接,用螺栓锁闭密封(注:密封箱体大小以将能容纳12个层叠的不锈钢方盘为准,见附图)。Horizontal rectangular pressure steam sterilizer (specification: 30L, 1018×500×600 mm); constant temperature incubator (specification: 750×600×600 mm); ultra-clean workbench (specification: 1400×690×520 mm); Large-capacity oscillator; stainless steel sealed box multi-layer square plate, including: 12 stainless steel square plates, length, width and height 60×45×2.0㎝; 1 stainless steel sealed box, length, width and height 60×45×24㎝; sealed 1 cover, length and width 49×28㎝, two inoculation holes that can be sealed with silicone plugs are set at the opposite corners of the sealing cover surface, and the sealing cover is connected with the box body with the help of silicone pads, and the sealing is sealed with bolts (note: sealing The size of the box is subject to the ability to accommodate 12 stacked stainless steel square plates, see attached picture).
2)培养基制备2) Culture medium preparation
营养琼脂培养基:蛋白胨0.1 kg;牛肉膏0.03 kg;氯化钠0.05 kg;琼脂0.15 kg;蒸馏水10 L。Nutrient agar medium: peptone 0.1 kg; beef extract 0.03 kg; sodium chloride 0.05 kg; agar 0.15 kg; distilled water 10 L.
将培养基混匀,用10%氢氧化钠调节至pH7.4,通过密封箱的接种孔将培养基注入密封箱,用硅胶塞密封接种孔,置121 ℃高压灭菌15 min,待箱体温度降至50℃~60℃,震荡箱体混匀培养基,以方盘位置为基准竖立箱体静置片刻,使琼胶从缝隙中流入方盘,然后快速水平放置箱体并使方盘朝上,使融化的营养琼脂均匀分布于每个方盘中,待琼脂降温凝固,形成厚度为3 mm~5 mm营养琼脂凝胶备用。Mix the medium evenly, adjust the pH to 7.4 with 10% sodium hydroxide, inject the medium into the sealed box through the inoculation hole of the sealed box, seal the inoculated hole with a silica gel plug, and put it at 121 ℃ for 15 minutes to autoclave, and wait for the box to Lower the temperature to 50°C-60°C, shake the box to mix the culture medium, stand the box upright based on the position of the square plate and let the agar flow into the square plate from the gap, then quickly place the box horizontally and make the square plate Facing upward, distribute the melted nutrient agar evenly in each square plate, wait for the agar to cool down and solidify, and form a nutrient agar gel with a thickness of 3 mm to 5 mm for later use.
3) 接种培养3) Inoculation culture
借助超净工作台,通过无菌术式经密封箱的接种孔接入大肠埃希氏菌C600菌种1000 ml,菌种浓度为5亿个/ml,硅胶塞密封接种孔。以方盘位置为基准竖立箱体静置片刻使菌液从缝隙中流入方盘,待菌种液面平衡稳定,快速水平放置箱体并使方盘朝上,轻轻倾斜、往返震荡箱体使液体菌种充分涂布于琼脂培养基表面,置37 ℃培养36 h, 使菌种生长形成菌苔。With the help of an ultra-clean workbench, insert 1000 ml of Escherichia coli C600 strains through the inoculation hole of the sealed box through aseptic surgery, with a strain concentration of 500 million/ml, and seal the inoculation hole with a silica gel plug. Take the position of the square plate as the reference to erect the box and let it stand for a while to allow the bacteria liquid to flow into the square plate from the gap. After the liquid level of the bacteria is balanced and stable, quickly place the box horizontally with the square plate facing upwards, gently tilt and vibrate the box back and forth The liquid strains were fully spread on the surface of the agar medium, and cultured at 37 °C for 36 h to allow the strains to grow and form a lawn.
4)菌液收集4) Bacterial liquid collection
通过无菌术式经密封箱的接种孔注入灭菌生理盐水10 L,密封接种孔后将箱体置于振荡机上,50次/min震荡15 min,充分洗涤菌苔,导出洗涤液至无菌容器,获得约10 L浓度为1500亿个/ml的浓缩菌液。Inject 10 L of sterilized physiological saline through the inoculation hole of the sealed box through the aseptic method, seal the inoculation hole, place the box on a shaker, shake at 50 times/min for 15 minutes, fully wash the bacterial lawn, and export the washing liquid to aseptic container to obtain about 10 L of concentrated bacterial liquid with a concentration of 150 billion cells/ml.
5)主要设备投资、生产成本5) Major equipment investment and production cost
设备器材:5.5万元(蒸汽灭菌器2.8万元;恒温培养箱1万元;超净工作台1.2万元;大容量振荡器0.3万元;密封箱体多层方盘2000元)Equipment and equipment: 55,000 yuan (28,000 yuan for a steam sterilizer; 10,000 yuan for a constant temperature incubator; 12,000 yuan for an ultra-clean workbench; 3,000 yuan for a large-capacity oscillator; 2,000 yuan for a sealed multi-layer square plate)
培养基:44.6元(蛋白胨0.1 kg×200元;牛肉膏0.03 kg×300元;氯化Medium: 44.6 yuan (peptone 0.1 kg×200 yuan; beef extract 0.03 kg×300 yuan; chlorinated
钠0.05 kg×12元;琼脂0.15 kg×100元)。Sodium 0.05 kg×12 yuan; agar 0.15 kg×100 yuan).
水电费:34元(灭菌5KV×3 h×1元;培养0.5 KV×36/2 h×1元;蒸馏Utilities: 34 yuan (sterilization 5KV×3 h×1 yuan; culture 0.5 KV×36/2 h×1 yuan; distillation
水10 L×1元;器材洗涤用自来水200 L)。10 L of water x 1 yuan; 200 L of tap water for equipment washing).
人员工资:200元(1人×1 d×200元)。Staff salary: 200 yuan (1 person x 1 d x 200 yuan).
6)废物排放6) Waste discharge
废弃培养基10 L;器材洗刷用自来水200 L。10 L of discarded culture medium; 200 L of tap water for equipment washing.
将实施例1、实施例2、实施例3的三种发酵培养方法进行比较Three kinds of fermentation culture methods of embodiment 1, embodiment 2, embodiment 3 are compared
发酵罐液体培养方法,设备投入高(10.2万元),发酵培养工艺简单,原料成本较高,菌液浓缩工艺繁琐、人员劳动强度大、产品易污染,材料消耗成本高。The fermentation tank liquid culture method requires high equipment investment (102,000 yuan), simple fermentation culture process, high raw material cost, cumbersome bacterial liquid concentration process, high labor intensity, easy pollution of products, and high material consumption cost.
茄形瓶营养琼脂平面培养方法,设备投入较高(6.7万元),发酵培养、收获工艺繁琐、人员劳动强度大、产品易污染,材料消耗成本较低。The eggplant-shaped bottle nutrient agar planar culture method requires high equipment investment (67,000 yuan), cumbersome fermentation culture and harvesting processes, high labor intensity, easy pollution of products, and low material consumption costs.
多层方盘固体平面培养方法,设备投入较低(5.5万元),发酵培养、收获工艺简单,人员劳动强度低,产品污染机率低,材料消耗成本较低。具体见表1。The multi-layer square plate solid plane culture method has low equipment investment (55,000 yuan), simple fermentation culture and harvesting process, low labor intensity of personnel, low probability of product pollution, and low material consumption cost. See Table 1 for details.
表1 三种发酵培养方法生产10 L浓缩菌液主要成本比较表Table 1 Comparison of main costs of producing 10 L concentrated bacterial liquid by three fermentation methods
实施例4Example 4
通辽市某大型养猪场因生产需要,培养大量大肠杆菌k88、k99基因工程菌,利用液体培养方法和茄形瓶营养琼脂平面培养方法,但产品污染较多,培养物的成品率较低,不能满足生产需求。应用多层方盘固体平面培养方法后,降低了人员劳动强度和产品污染机率,培养物的成品率显著提高,累计生产大肠杆菌k88、k99基因工程菌浓缩菌液数吨,取得了良好的生产效益。应用多层方盘固体平面培养制备大肠杆菌k88、k99基因工程菌的所需设备和具体操作方法如下:A large pig farm in Tongliao City cultivated a large number of Escherichia coli k88 and k99 genetically engineered bacteria due to production needs, using liquid culture methods and eggplant-shaped bottle nutrient agar plane culture methods, but the products were more polluted and the yield of the cultures was low. Can not meet production needs. After applying the multi-layer square plate solid plane culture method, the labor intensity of personnel and the probability of product contamination have been reduced, and the yield of culture products has been significantly improved. The accumulative production of Escherichia coli k88 and k99 genetically engineered bacteria concentrates several tons, and good production benefit. The required equipment and specific operation methods for preparing Escherichia coli k88 and k99 genetically engineered bacteria by using multi-layer square plate solid plane culture are as follows:
1) 设备1) Equipment
卧式矩形压力蒸汽灭菌器、恒温培养箱、超净工作台、振荡器、不锈钢密封箱和多层方盘(包括:不锈钢方盘12个,长宽高60×45×2.0㎝;不锈钢密封箱体1个,长宽高60×45×24㎝;密封盖1个,长宽49×28㎝),密封盖表面对角处分别设置2个可用硅胶塞密封的接种孔操作,借助硅胶垫将密封盖和箱体连接,用螺栓锁闭密封。Horizontal rectangular pressure steam sterilizer, constant temperature incubator, ultra-clean workbench, oscillator, stainless steel sealed box and multi-layer square plate (including: 12 stainless steel square plates, length, width and height 60×45×2.0㎝; stainless steel seal 1 box, length, width and height 60×45×24㎝; 1 sealing cover, length and width 49×28㎝), two inoculation holes that can be sealed with silicone plugs are set at the opposite corners of the sealing cover surface, and the operation is performed with the help of silicone pads Connect the sealing cover and the box body, and lock and seal with bolts.
2)培养基制备2) Culture medium preparation
营养琼脂培养基:蛋白胨0.1 kg;牛肉膏0.03 kg;氯化钠0.05 kg;琼脂0.15 kg;蒸馏水10 L。Nutrient agar medium: peptone 0.1 kg; beef extract 0.03 kg; sodium chloride 0.05 kg; agar 0.15 kg; distilled water 10 L.
将培养基各组分混匀,用10%氢氧化钠调节至pH7.4,通过密封箱的接种孔将培养基注入密封箱,用硅胶塞密封接种孔,置121 ℃高压灭菌15 min,待箱体温度降至50 ℃~60 ℃,震荡箱体混匀培养基,以方盘位置为基准竖立箱体静置片刻,使琼胶从缝隙中流入方盘,然后快速水平放置箱体并使方盘朝上,使融化的营养琼脂均匀分布于每个方盘中,待琼脂降温凝固,形成厚度为3 mm~5 mm 营养琼脂凝胶备用。Mix the components of the culture medium evenly, adjust the pH to 7.4 with 10% sodium hydroxide, inject the culture medium into the sealed box through the inoculation hole of the sealed box, seal the inoculated hole with a silica gel plug, and place it at 121 °C for 15 minutes to autoclave. When the temperature of the box drops to 50 ℃ ~ 60 ℃, shake the box to mix the culture medium, stand the box upright based on the position of the square plate for a while, let the agar flow into the square plate from the gap, and then quickly place the box horizontally and Make the square plates face up, and distribute the melted nutrient agar evenly in each square plate, wait for the agar to cool down and solidify, and form a nutrient agar gel with a thickness of 3 mm to 5 mm for later use.
3) 接种培养3) Inoculation culture
借助超净工作台,通过无菌术式经密封箱的接种孔接入大肠杆菌k88、k99基因工程菌菌种液1000 ml,菌种浓度保持5亿个/ml以上,硅胶塞密封接种孔。以方盘位置为基准竖立箱体静置片刻使菌液从缝隙中流入方盘,待菌种液面平衡稳定,快速水平放置箱体并使方盘朝上,轻轻倾斜、往返震荡箱体使液体菌种充分涂布于琼脂培养基表面,置37 ℃培养48 h, 使菌种生长形成菌苔。With the help of an ultra-clean workbench, 1000 ml of Escherichia coli k88 and k99 genetically engineered strains were inserted through the inoculation hole of the sealed box through aseptic surgery. The concentration of the strain was kept above 500 million/ml, and the inoculation hole was sealed with a silica gel plug. Take the position of the square plate as the reference to erect the box and let it stand for a while to allow the bacteria liquid to flow into the square plate from the gap. After the liquid level of the bacteria is balanced and stable, quickly place the box horizontally with the square plate facing upwards, gently tilt and vibrate the box back and forth The liquid strains were fully spread on the surface of the agar medium, and cultured at 37 °C for 48 h to allow the strains to grow and form a lawn.
4)菌液收集4) Bacterial liquid collection
通过无菌术式经密封箱的接种孔注入灭菌生理盐水10 L,密封接种孔后将箱体置于振荡机上,50次/min震荡15 min,充分洗涤菌苔,导出洗涤液至无菌容器,获得10 L浓度约为1500亿个/ml的浓缩菌液。Inject 10 L of sterilized physiological saline through the inoculation hole of the sealed box through the aseptic method, seal the inoculation hole, place the box on a shaker, shake at 50 times/min for 15 minutes, fully wash the bacterial lawn, and export the washing liquid to aseptic container to obtain 10 L of concentrated bacterial liquid with a concentration of about 150 billion cells/ml.
以上所述仅为本发明的较佳实施例,凡依本发明申请专利范围所做的均等变化与修饰,皆应属本发明的涵盖范围。The above descriptions are only preferred embodiments of the present invention, and all equivalent changes and modifications made according to the scope of the patent application of the present invention shall fall within the scope of the present invention.
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3715280A (en) * | 1970-07-14 | 1973-02-06 | Us Health | Mini-test dish |
WO1989011529A1 (en) * | 1988-05-23 | 1989-11-30 | The Regents Of The University Of Minnesota | Bioreactor device |
GB2346379A (en) * | 1999-02-08 | 2000-08-09 | Biodiversity Ltd | Growing organisms in a multi-compartment vessel |
US20030157706A1 (en) * | 2002-02-15 | 2003-08-21 | Carol Hamilton | High throughput method, apparatus and kit for plating microorganisms and cell cultures |
CN1212385C (en) * | 1998-04-30 | 2005-07-27 | 普洛菲塔生化植物保护有限公司 | Solid-state fermenter and process for solid-state fermentaion |
CN102827755A (en) * | 2011-06-15 | 2012-12-19 | 天津市恒明石英玻璃制品有限公司 | Modular biological incubator |
CN204550529U (en) * | 2015-04-02 | 2015-08-12 | 南阳医学高等专科学校 | A kind of microbial cultivation device |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3715280A (en) * | 1970-07-14 | 1973-02-06 | Us Health | Mini-test dish |
WO1989011529A1 (en) * | 1988-05-23 | 1989-11-30 | The Regents Of The University Of Minnesota | Bioreactor device |
CN1212385C (en) * | 1998-04-30 | 2005-07-27 | 普洛菲塔生化植物保护有限公司 | Solid-state fermenter and process for solid-state fermentaion |
GB2346379A (en) * | 1999-02-08 | 2000-08-09 | Biodiversity Ltd | Growing organisms in a multi-compartment vessel |
US20030157706A1 (en) * | 2002-02-15 | 2003-08-21 | Carol Hamilton | High throughput method, apparatus and kit for plating microorganisms and cell cultures |
CN102827755A (en) * | 2011-06-15 | 2012-12-19 | 天津市恒明石英玻璃制品有限公司 | Modular biological incubator |
CN204550529U (en) * | 2015-04-02 | 2015-08-12 | 南阳医学高等专科学校 | A kind of microbial cultivation device |
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