CN116064458A - Method for extracting glutamine transaminase by using polyethylene glycol - Google Patents
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Abstract
本发明公开了一种采用聚乙二醇提取谷氨酰胺转氨酶的方法,包括以下步骤:步骤一,制备发酵液;步骤二,过滤浓缩;步骤三,提取谷氨酰胺转氨酶;步骤四,获取谷氨酰胺转氨酶粗品;步骤五,制备谷氨酰胺转氨酶成品;所述步骤二中,浓缩液中谷氨酰胺转氨酶活性约100U/ml;所述步骤三中,聚乙二醇的质量百分比浓度为5%‑50%;所述步骤三中,静置时间为24h;所述步骤五中,合格品的混合物酶活性为100u/g±10%;本发明采用聚乙二醇提取茂原链霉菌发酵液中的谷氨酰胺转氨酶,克服了现有技术中有机媒溶沉淀法和盐析法的缺陷,工艺更为简单安全,且对环境友好,具有提取收率高、生产成本低的优点,为其更广泛的使用提供有利条件。
The invention discloses a method for extracting glutamine transaminase by using polyethylene glycol, which comprises the following steps: step 1, preparing fermented liquid; step 2, filtering and concentrating; step 3, extracting glutamine transaminase; step 4, obtaining glutamine transaminase Transaminase crude product; step five, preparing finished product of transaminase; in step two, the activity of transaminase in the concentrate is about 100U/ml; in step three, the mass percentage concentration of polyethylene glycol is 5% -50%; in the step three, the standing time is 24h; in the step five, the mixed enzyme activity of the qualified product is 100u/g ± 10%; the present invention adopts polyethylene glycol to extract Streptomyces mobara fermentation broth The transglutaminase, which overcomes the defects of the organic solvent precipitation method and salting out method in the prior art, has a simpler and safer process, is environmentally friendly, has the advantages of high extraction yield and low production cost, and is more Widespread use offers advantages.
Description
技术领域technical field
本发明涉及生物酶制剂生产技术领域,具体为一种采用聚乙二醇提取谷氨酰胺转氨酶的方法。The invention relates to the technical field of production of biological enzyme preparations, in particular to a method for extracting glutamine transaminase by using polyethylene glycol.
背景技术Background technique
谷氨酰胺转氨酶广泛存在于动物(包括人类)、植物和微生物中。它是一种酰基转移酶,通过催化蛋白质分子间及分子内发生酰基转移反应,从而引起蛋白质(或多肽)之间发生共价交联。这种交联对蛋白质的性质、凝胶能力、热稳定性和持水力等有显著影响,从而改善蛋白质食品的起泡性、可塑性、持水性;并且能催化各种必需氨基酸与蛋白质的交联,能提高蛋白质的营养价值。由于其高度的专一性和安全性、卓越的交联特性,它被广泛地运用在肉制品、水产品、豆制品、面制品、米制品和乳制品等食品加工业中。近年来随着对此酶应用的深入研究,发现它在医药、日用化工、制革、纺织等领域均有广泛用途。Transglutaminase widely exists in animals (including humans), plants and microorganisms. It is an acyltransferase that catalyzes acyl transfer reactions between protein molecules and within molecules, thereby causing covalent cross-linking between proteins (or polypeptides). This kind of cross-linking has a significant impact on the properties, gel ability, thermal stability and water-holding capacity of proteins, thereby improving the foamability, plasticity and water-holding capacity of protein foods; and can catalyze the cross-linking of various essential amino acids and proteins , can improve the nutritional value of protein. Due to its high specificity, safety and excellent cross-linking properties, it is widely used in food processing industries such as meat products, aquatic products, soybean products, flour products, rice products and dairy products. In recent years, with the in-depth research on the application of this enzyme, it has been found that it has a wide range of applications in the fields of medicine, daily chemical industry, tanning, and textiles.
在现有技术中,关于谷氨酰胺转氨酶的提取方法包括以下两种:一是有机媒溶沉淀法:即采用乙醇沉淀或丙酮沉淀法。此法虽然简单,但生产过程中使用了易燃易爆物质,存在严重的安全隐患;二是盐析法:即采用饱和硫酸铵、饱和硫酸钠、饱和氯化钠等盐析,使用此法得到的沉淀物要用大量纯水透析脱盐,然后才能在食品加工业或其它行业中应用,工艺较为复杂。In the prior art, the extraction methods for transglutaminase include the following two types: one is the organic solvent precipitation method: that is, ethanol precipitation or acetone precipitation method is used. Although this method is simple, flammable and explosive substances are used in the production process, and there are serious safety hazards; the second is the salting-out method: that is, saturated ammonium sulfate, saturated sodium sulfate, saturated sodium chloride, etc. are used for salting-out. The obtained precipitate must be dialyzed and desalted with a large amount of pure water before it can be used in the food processing industry or other industries, and the process is relatively complicated.
发明内容Contents of the invention
本发明的目的在于提供一种采用聚乙二醇提取谷氨酰胺转氨酶的方法,以解决上述背景技术中提出的问题。The object of the present invention is to provide a method for extracting transglutaminase using polyethylene glycol, so as to solve the problems raised in the above-mentioned background technology.
为实现上述目的,本发明提供如下技术方案:一种采用聚乙二醇提取谷氨酰胺转氨酶的方法,包括以下步骤:步骤一,制备发酵液;步骤二,过滤浓缩;步骤三,提取谷氨酰胺转氨酶;步骤四,获取谷氨酰胺转氨酶粗品;步骤五,制备谷氨酰胺转氨酶成品;To achieve the above object, the present invention provides the following technical solutions: a method for extracting transglutaminase using polyethylene glycol, comprising the following steps: Step 1, preparing fermentation broth; Step 2, filtering and concentrating; Step 3, extracting glutamine Amide transaminase; Step 4, obtaining the crude product of Transglutaminase; Step 5, preparing the finished product of Transglutaminase;
其中在上述步骤一中,具体包括以下步骤:Wherein in the above-mentioned step 1, specifically include the following steps:
1.1制备种子液:取茂原链霉菌孢子接种于含种子培养基的种子罐中,培养24-48h后,得到种子液;1.1 Preparation of seed liquid: inoculate the spores of Streptomyces mobara into the seed tank containing the seed medium, and cultivate for 24-48 hours to obtain the seed liquid;
1.2制备发酵液:将种子液接种于内装发酵培养基的发酵罐中,培养40-60h后,得到发酵液;1.2 Preparation of fermentation liquid: inoculate the seed liquid in a fermenter with a built-in fermentation medium, and cultivate for 40-60 hours to obtain a fermentation liquid;
其中在上述步骤二中,取步骤1.2中制备的发酵液,经板框过滤后,得到滤液,将滤液经微滤和超滤处理,浓缩5-10倍后得到浓缩液;Wherein in the above step 2, the fermented liquid prepared in step 1.2 is taken, filtered through a plate and frame to obtain a filtrate, and the filtrate is subjected to microfiltration and ultrafiltration, and concentrated 5-10 times to obtain a concentrated solution;
其中在上述步骤三中,在10-15℃条件下,取步骤二中制备的浓缩液,一边向其中加入聚乙二醇,一边进行搅拌,当聚乙二醇完全溶解后,静置一段时间,弃上清液后离心,得到谷氨酰胺转氨酶沉淀物;Among them, in the above step three, under the condition of 10-15°C, take the concentrated solution prepared in step two, add polyethylene glycol to it while stirring, and when the polyethylene glycol is completely dissolved, let it stand for a period of time , discard the supernatant and centrifuge to obtain a transglutaminase precipitate;
其中在上述步骤四中,取步骤三中制备的谷氨酰胺转氨酶沉淀物,经冷冻干燥处理后,得到谷氨酰胺转氨酶粗品;Wherein in the above step 4, the transglutaminase precipitate prepared in step 3 is taken, and after freeze-drying treatment, the crude product of transglutaminase is obtained;
其中在上述步骤五中,取步骤四中制备的谷氨酰胺转氨酶粗品,按照产品要求加入一定量载体,充分混合后测定混合物酶活性,合格品包装贮存。Wherein in the above step 5, the crude transglutaminase prepared in the step 4 is taken, a certain amount of carrier is added according to the product requirements, the enzyme activity of the mixture is determined after fully mixing, and qualified products are packaged and stored.
优选的,所述步骤1.1中,培养条件为:培养温度28-30℃;搅拌转速100-250转/分;通气量1:0.3-0.6(v/v)。Preferably, in the step 1.1, the culture conditions are: culture temperature 28-30°C; stirring speed 100-250 rpm; ventilation rate 1:0.3-0.6 (v/v).
优选的,所述步骤1.2中,培养条件为:培养温度28-30℃;搅拌转速100-200转/分;通气量1:0.5-0.8(v/v)。Preferably, in the step 1.2, the culture conditions are: culture temperature 28-30° C.; stirring speed 100-200 rpm; ventilation rate 1:0.5-0.8 (v/v).
优选的,所述步骤二中,浓缩液中谷氨酰胺转氨酶活性约100U/ml。Preferably, in the second step, the activity of transglutaminase in the concentrate is about 100 U/ml.
优选的,所述步骤三中,聚乙二醇的质量百分比浓度为5%-50%。Preferably, in the step 3, the mass percent concentration of polyethylene glycol is 5%-50%.
优选的,所述步骤三中,静置时间为24h。Preferably, in said step 3, the standing time is 24h.
优选的,所述步骤五中,合格品的混合物酶活性为100u/g±10%。Preferably, in the step five, the mixed enzyme activity of the qualified product is 100u/g±10%.
优选的,所述步骤五中,包装规格为1kg/袋。Preferably, in said step five, the packaging specification is 1kg/bag.
优选的,所述步骤五中,载体为淀粉和糊精。Preferably, in the fifth step, the carrier is starch and dextrin.
与现有技术相比,本发明的有益效果是:本发明采用聚乙二醇提取茂原链霉菌发酵液中的谷氨酰胺转氨酶,克服了现有技术中有机媒溶沉淀法和盐析法的缺陷,工艺更为简单安全,且对环境友好,具有提取收率高、生产成本低的优点,为其更广泛的使用提供有利条件。Compared with the prior art, the beneficial effects of the present invention are: the present invention uses polyethylene glycol to extract the transglutaminase in the Streptomyces mobara fermentation broth, which overcomes the limitations of the organic solvent precipitation method and the salting-out method in the prior art. Defects, the process is simpler and safer, and it is environmentally friendly. It has the advantages of high extraction yield and low production cost, providing favorable conditions for its wider use.
附图说明Description of drawings
图1为本发明的方法流程图。Fig. 1 is a flow chart of the method of the present invention.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
请参阅图1,本发明提供的一种技术方案:Please refer to Fig. 1, a kind of technical scheme provided by the present invention:
实施例1Example 1
一种采用聚乙二醇提取谷氨酰胺转氨酶的方法,包括以下步骤:步骤一,制备发酵液;步骤二,过滤浓缩;步骤三,提取谷氨酰胺转氨酶;步骤四,获取谷氨酰胺转氨酶粗品;步骤五,制备谷氨酰胺转氨酶成品;A method for extracting transglutaminase by using polyethylene glycol, comprising the following steps: step 1, preparing fermentation broth; step 2, filtering and concentrating; step 3, extracting transglutaminase; step 4, obtaining crude transglutaminase ; Step 5, preparing the finished product of transglutaminase;
其中在上述步骤一中,具体包括以下步骤:Wherein in the above-mentioned step 1, specifically include the following steps:
1.1制备种子液:取茂原链霉菌孢子接种于含种子培养基的种子罐中,培养48h后,得到种子液;其中,培养条件为:培养温度28-30℃;1.1 Preparation of seed liquid: Inoculate the spores of Streptomyces mobara into the seed tank containing the seed medium, and cultivate for 48 hours to obtain the seed liquid; wherein, the culture conditions are: culture temperature 28-30°C;
搅拌转速100-250转/分;通气量1:0.3-0.6(v/v);Stirring speed 100-250 rpm; ventilation volume 1:0.3-0.6(v/v);
1.2制备发酵液:将种子液接种于内装发酵培养基的发酵罐中,培养60h后,得到发酵液;其中,培养条件为:培养温度28-30℃;搅拌转速100-200转/分;通气量1:0.5-0.8(v/v);1.2 Preparation of fermentation liquid: inoculate the seed liquid into a fermenter with a built-in fermentation medium, and cultivate for 60 hours to obtain a fermentation liquid; wherein, the culture conditions are: culture temperature 28-30°C; stirring speed 100-200 rpm; ventilation Volume 1: 0.5-0.8(v/v);
其中在上述步骤二中,取步骤1.2中制备的发酵液,经板框过滤后,得到滤液,将滤液经微滤和超滤处理,浓缩5-10倍后得到浓缩液,浓缩液中谷氨酰胺转氨酶活性约100U/ml;Wherein in the above step 2, the fermented liquid prepared in step 1.2 is taken, and after plate and frame filtration, the filtrate is obtained, and the filtrate is processed by microfiltration and ultrafiltration, and concentrated 5-10 times to obtain a concentrated solution, in which glutamine The transaminase activity is about 100U/ml;
其中在上述步骤三中,在10-15℃条件下,取步骤二中制备的浓缩液10L,一边向其中加入1kg食品级聚乙二醇400,一边进行搅拌,当食品级聚乙二醇400完全溶解后,静置24h,弃上清液后离心,得到谷氨酰胺转氨酶沉淀物;Wherein in the above step three, under the condition of 10-15°C, take 10L of the concentrated solution prepared in step two, and add 1kg of food-grade polyethylene glycol 400 to it while stirring, when the food-grade polyethylene glycol 400 After completely dissolving, let it stand for 24 hours, discard the supernatant and centrifuge to obtain the transglutaminase precipitate;
其中在上述步骤四中,取步骤三中制备的谷氨酰胺转氨酶沉淀物,经冷冻干燥处理后,得到谷氨酰胺转氨酶粗品;Wherein in the above step 4, the transglutaminase precipitate prepared in step 3 is taken, and after freeze-drying treatment, the crude product of transglutaminase is obtained;
其中在上述步骤五中,取步骤四中制备的谷氨酰胺转氨酶粗品,按照产品要求加入一定量的淀粉和糊精,充分混合后测定混合物酶活性,合格品包装贮存;其中,合格品的混合物酶活性为100u/g±10%,包装规格为1kg/袋。Wherein in above-mentioned step 5, get the transglutaminase crude product prepared in step 4, add a certain amount of starch and dextrin according to product requirements, measure the enzymatic activity of mixture after fully mixing, qualified product is packaged and stored; Wherein, the mixture of qualified product The enzyme activity is 100u/g±10%, and the packaging specification is 1kg/bag.
实施例2Example 2
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400的添加量改为2kg。The extraction method of transglutaminase was the same as in Example 1, except that the amount of food-grade polyethylene glycol 400 added in step 3 was changed to 2kg.
实施例3Example 3
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400的添加量改为3kg。The extraction method of transglutaminase was the same as in Example 1, except that the amount of food-grade polyethylene glycol 400 added in step 3 was changed to 3kg.
实施例4Example 4
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇2000。The extraction method of transglutaminase was the same as in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 2000.
实施例5Example 5
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇2000,将添加量改为2kg。The extraction method of transglutaminase was the same as that in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 2000, and the addition amount was changed to 2kg.
实施例6Example 6
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇2000,将添加量改为3kg。The extraction method of transglutaminase was the same as that in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 2000, and the addition amount was changed to 3kg.
实施例7Example 7
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇4000。The extraction method of transglutaminase was the same as in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 4000.
实施例8Example 8
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇4000,将添加量改为2kg。The extraction method of transglutaminase was the same as that in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 4000, and the addition amount was changed to 2kg.
实施例9Example 9
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇4000,将添加量改为3kg。The extraction method of transglutaminase was the same as that in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 4000, and the addition amount was changed to 3kg.
实施例10Example 10
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇8000。The extraction method of transglutaminase was the same as in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 8000.
实施例11Example 11
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇8000,将添加量改为2kg。The extraction method of transglutaminase was the same as that in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 8000, and the addition amount was changed to 2 kg.
实施例12Example 12
谷氨酰胺转氨酶的提取方法与实施例1相同,只将步骤三中食品级聚乙二醇400改为食品级聚乙二醇8000,将添加量改为3kg。The extraction method of transglutaminase was the same as that in Example 1, except that the food-grade polyethylene glycol 400 in step 3 was changed to food-grade polyethylene glycol 8000, and the addition amount was changed to 3kg.
基于上述,本发明的优点在于,该发明通过在茂原链霉菌发酵液的浓缩液中添加一定浓度的聚乙二醇,使浓缩液中的谷氨酰胺转氨酶沉淀,再通过液固分离得到固态的谷氨酰胺转氨酶;该过程不使用有机溶媒如乙醇、丙酮;不使用盐析如饱和硫酸铵、硫化钠、氯化钠;也不使用有机酸,因此生产工艺简单安全,且对环境友好。Based on the above, the advantage of the present invention is that the invention adds a certain concentration of polyethylene glycol to the concentrated solution of Streptomyces mobara fermentation broth, so that the transglutaminase in the concentrated solution is precipitated, and then solid-state transglutaminase is obtained by liquid-solid separation. Transglutaminase; this process does not use organic solvents such as ethanol and acetone; does not use salting out such as saturated ammonium sulfate, sodium sulfide, sodium chloride; and does not use organic acids, so the production process is simple, safe and environmentally friendly.
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 invention is not limited to the details of the above-described exemplary embodiments, but that the invention can be embodied in other specific forms without departing from the spirit or essential characteristics of the invention. Accordingly, the embodiments should be regarded in all points of view as exemplary and not restrictive, the scope of the invention being defined by the appended claims rather than the foregoing description, and it is therefore intended that the scope of the invention be defined by the appended claims rather than by the foregoing description. All changes within the meaning and range of equivalents of the elements are embraced in the present invention. Any reference sign in a claim should not be construed as limiting the claim concerned.
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