CN105624242A - Method for preparing active peptide through high-temperature fermentation of aquatic protein - Google Patents
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- 241000252203 Clupea harengus Species 0.000 claims description 4
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- 241000237509 Patinopecten sp. Species 0.000 claims description 3
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- 241000962514 Alosa chrysochloris Species 0.000 claims description 2
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- 241000252230 Ctenopharyngodon idella Species 0.000 claims description 2
- 241000252234 Hypophthalmichthys nobilis Species 0.000 claims description 2
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- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000003627 anti-cholesterol Effects 0.000 description 1
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- 239000001168 astaxanthin Substances 0.000 description 1
- MQZIGYBFDRPAKN-ZWAPEEGVSA-N astaxanthin Chemical compound C([C@H](O)C(=O)C=1C)C(C)(C)C=1/C=C/C(/C)=C/C=C/C(/C)=C/C=C/C=C(C)C=CC=C(C)C=CC1=C(C)C(=O)[C@@H](O)CC1(C)C MQZIGYBFDRPAKN-ZWAPEEGVSA-N 0.000 description 1
- 229940022405 astaxanthin Drugs 0.000 description 1
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- 230000007812 deficiency Effects 0.000 description 1
- KCIDZIIHRGYJAE-YGFYJFDDSA-L dipotassium;[(2r,3r,4s,5r,6r)-3,4,5-trihydroxy-6-(hydroxymethyl)oxan-2-yl] phosphate Chemical compound [K+].[K+].OC[C@H]1O[C@H](OP([O-])([O-])=O)[C@H](O)[C@@H](O)[C@H]1O KCIDZIIHRGYJAE-YGFYJFDDSA-L 0.000 description 1
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- 235000013619 trace mineral Nutrition 0.000 description 1
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
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Abstract
Description
技术领域technical field
本发明涉及一种利用水产蛋白高温发酵制备活性肽的方法,属于水产品加工与利用的领域。The invention relates to a method for preparing active peptides through high-temperature fermentation of aquatic proteins, belonging to the field of processing and utilization of aquatic products.
背景技术Background technique
蛋白质酶解的后的产物小肽不但容易消化、吸收,而且还具有抗高血压、抗胆固醇、抗血栓形成、改善脂质代谢、增强人体体能、帮助恢复疲劳、促进钙磷和其它微量元素的吸收、促进大脑发育、提高记忆力、增强巨噬细胞和B细胞活力、增强免疫功能、保护表皮细胞、防止黑色素沉淀、消除体内自由基等功效。The small peptides produced by protein enzymatic hydrolysis are not only easy to digest and absorb, but also have anti-hypertensive, anti-cholesterol, anti-thrombosis, improve lipid metabolism, enhance human physical fitness, help restore fatigue, promote calcium, phosphorus and other trace elements. Absorption, promote brain development, improve memory, enhance the vitality of macrophages and B cells, enhance immune function, protect epidermal cells, prevent melanin precipitation, eliminate free radicals in the body, etc.
关于水产蛋白活性肽的制备,国内进行了大量的研究。目前,水产蛋白活性肽的制备方法主要有自溶酶解、酶解法、液态发酵法和固态发酵与液态酶解相结合的方法这四种。专利申请200810195646.4“内源酶制备生物活性小肽的工艺”公开了一种利用海洋低值鱼体内的内源酶自溶酶解的方法制备水产蛋白生物活性小肽的方法。专利申请201410145196.3“一种制备扇贝裙边活性肽的方法”公开了一种酶解法制备水产蛋白活性肽的方法。专利申请CN102028091A“一种纳豆菌发酵法制备低分子鱼肽的方法”公开了一种液体发酵法制备鱼蛋白肽的方法,专利申请201210539941.3“一种由鱼蛋白肽和与大豆肽组成的蛋白肽的生产方法”公开了一种由固态发酵与液态酶解相结合制备水产蛋白活性肽的方法。A lot of research has been done in China on the preparation of aquatic protein active peptides. At present, the preparation methods of aquatic protein active peptides mainly include autolytic enzymatic hydrolysis, enzymatic hydrolysis, liquid fermentation and solid-state fermentation combined with liquid enzymatic hydrolysis. Patent application 200810195646.4 "Process of preparing small biologically active peptides with endogenous enzymes" discloses a method for preparing small biologically active peptides from aquatic proteins by using endogenous enzymes in marine low-value fish to autolyze and enzymolyze. Patent application 201410145196.3 "A method for preparing scallop skirt active peptide" discloses a method for preparing aquatic protein active peptide by enzymatic hydrolysis. Patent application CN102028091A "A Method for Preparing Low Molecular Fish Peptides by Bacteria Natto Fermentation" discloses a method for preparing fish protein peptides by liquid fermentation. Patent application 201210539941.3 "A protein composed of fish protein peptides and soybean peptides Peptide Production Method" discloses a method for preparing aquatic protein active peptides by combining solid-state fermentation and liquid-state enzymatic hydrolysis.
现有的水产蛋白活性肽制备技术中存在以下缺陷。首先,现有的水产蛋白活性肽制备技术中都有高温处理的过程。以上制备技术中都有高温灭酶这一工序;微生物发酵的方法原料需要灭菌。以上这些高温处理,会在一定程度减弱制备的功能肽或水产蛋白本身所含功能性成分的生物学活性;另外高温处理会显著增强美拉德反应,使得酶解液颜色变深,为成品加工过程增加了负担。其次,外加酶酶解的方法需要外加蛋白酶,增加了成本;自溶酶解由于内源酶的不足,导致酶解不彻底。另外,微生物发酵法虽然不用外加蛋白酶,但是原料需要灭菌导致内源酶失活,不能充分地有效利用内源酶。The following deficiencies exist in the existing aquatic protein active peptide preparation technology. First of all, the existing techniques for the preparation of active peptides from aquatic proteins all have a process of high temperature treatment. All of the above preparation technologies have the process of high temperature inactivation of enzymes; the raw materials of the microbial fermentation method need to be sterilized. The above high-temperature treatments will weaken the biological activity of the prepared functional peptides or the functional components contained in the aquatic protein itself to a certain extent; in addition, the high-temperature treatment will significantly enhance the Maillard reaction, making the color of the enzymatic hydrolyzate darker, which is suitable for the finished product processing process adds to the burden. Secondly, the method of enzymatic hydrolysis with external enzymes requires the addition of proteases, which increases the cost; autolytic enzymatic hydrolysis is incomplete due to the lack of endogenous enzymes. In addition, although the microbial fermentation method does not require external proteases, the raw materials need to be sterilized to inactivate the endogenous enzymes, and the endogenous enzymes cannot be fully and effectively utilized.
发明内容Contents of the invention
针对现有的水产蛋白活性肽制备技术所存在的问题。本发明的主要目的是提供一种低温的制备水产蛋白活性肽的方法,以便更好地保留制备的功能肽和水产蛋白本身所含功能性成分的生物学活性。本发明的另一目的是提供一种发酵法制备活性肽的方法,使得微生物发酵与内源酶酶解过程能有机结合在一起。本发明还有一目的是简化活性肽的制备工序,降低其生产成本。The invention aims at the problems existing in the existing preparation technology of aquatic protein active peptides. The main purpose of the present invention is to provide a low-temperature method for preparing active peptides from aquatic proteins, so as to better retain the biological activity of the prepared functional peptides and the functional components contained in the aquatic proteins themselves. Another object of the present invention is to provide a method for preparing active peptides by fermentation, so that microbial fermentation and endogenous enzyme enzymatic hydrolysis can be organically combined. Another purpose of the present invention is to simplify the preparation process of the active peptide and reduce its production cost.
为了解决上述问题,本发明所采用的技术方案如下:一种利用水产蛋白高温发酵制备活性肽的方法,包括如下步骤:In order to solve the above problems, the technical scheme adopted in the present invention is as follows: a method for preparing active peptides by high-temperature fermentation of aquatic proteins, comprising the following steps:
(1)将斜面保藏的能产耐高温蛋白酶的地衣芽孢杆菌(Bacilluslicheniformis)HL-3接入到灭菌后冷却的LB液体培养基中,于55℃、150r/min培养12h,制备成地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液备用;(1) Insert Bacillus licheniformis HL-3, which is capable of producing thermostable protease, preserved on the slant into the LB liquid medium cooled after sterilization, and culture it at 55°C and 150r/min for 12h to prepare licheniformis spores Bacillus licheniformis HL-3 seed liquid for use;
(2)将新鲜的水产蛋白绞碎后备用;(2) Grind the fresh aquatic protein for later use;
(3)将步骤(2)制得的绞碎的水产蛋白放入到发酵罐中,并向发酵罐中加入水和营养物,混匀后得到发酵培养基;(3) Put the minced aquatic protein prepared in step (2) into a fermenter, add water and nutrients into the fermenter, and mix well to obtain a fermentation medium;
(4)往步骤(3)获得的发酵培养上接入步骤(1)所制备的地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液;(4) adding the Bacillus licheniformis HL-3 seed solution prepared in step (1) to the fermentation culture obtained in step (3);
(5)液态发酵过程的控制:发酵温度为55℃~60℃,无菌空气通入量为0.5vvm~2.5vvm,发酵罐的转速为150rpm~350rpm,发酵时间为42h~48h;(5) Control of the liquid fermentation process: the fermentation temperature is 55°C-60°C, the sterile air intake is 0.5vvm-2.5vvm, the rotation speed of the fermentation tank is 150rpm-350rpm, and the fermentation time is 42h-48h;
(6)成品处理:将步骤(5)得到的发酵液进行过滤去除沉淀而得到上清液;上清液通过截留分子量为5000道尔顿的超滤膜的超滤去除大分子蛋白质而得到透过液;透过液然后通过截留分子量为200道尔顿的纳滤膜的纳滤去除氨基酸而得到浓缩液;浓缩液经过冷冻干燥而制备得到活性肽成品。(6) Finished product treatment: filter the fermented liquid obtained in step (5) to remove sediment to obtain a supernatant; The permeated liquid is then filtered through a nanofiltration membrane with a molecular weight cut-off of 200 Daltons to remove amino acids to obtain a concentrated liquid; the concentrated liquid is freeze-dried to prepare a finished product of active peptide.
所述步骤(1)中所用的能产耐高温蛋白酶的地衣芽孢杆菌(Bacilluslicheniformis)HL-3已于2016年1月18日保藏于广东省微生物菌种保藏中心,保藏编号为GDMCCNo:60003,保藏地址为广州市先烈中路100号大院59号楼5楼广东省微生物研究所。The Bacillus licheniformis HL-3 capable of producing thermostable protease used in the step (1) has been preserved in the Guangdong Provincial Microbial Culture Collection Center on January 18, 2016, and the preservation number is GDMCCNo: 60003. The address is Guangdong Institute of Microbiology, 5th Floor, Building 59, Compound, No. 100 Xianlie Middle Road, Guangzhou City.
所述步骤(2)中的水产蛋白为罗非鱼下脚料、南极磷虾、虾头、扇贝裙边、鳕鱼下脚料、鱿鱼下脚料、青鳞鱼下脚料、青鱼下脚料、鲢鱼下脚料、草鱼下脚料和鲣鱼下脚料中的一种。The aquatic protein in the step (2) is tilapia leftovers, Antarctic krill, shrimp head, scallop skirt, cod leftovers, squid leftovers, herring leftovers, herring leftovers, silver carp leftovers , grass carp scraps and skipjack scraps.
所述步骤(3)中水产蛋白的加入量以添加的水产蛋白的质量占发酵培养基总质量百分比计,为10%~30%。所述步骤(3)中营养物为葡萄糖、食品级氯化钙、食品级氯化亚铁和食品级磷酸氢二钾组成的混合物。所述步骤(3)中的营养物的加入量以添加的营养物的质量占发酵培养基总质量百分比计,分别为:葡萄糖0.01%~5%,食品级氯化钙0.01%~5%,食品级氯化亚铁0.01%~5%,食品级磷酸氢二钾0.01%~5%。The amount of aquatic protein added in the step (3) is 10% to 30% based on the mass percentage of the added aquatic protein in the total mass of the fermentation medium. The nutrient in the step (3) is a mixture composed of glucose, food-grade calcium chloride, food-grade ferrous chloride and food-grade dipotassium hydrogen phosphate. The amount of nutrients added in the step (3) is based on the weight of the added nutrients as a percentage of the total mass of the fermentation medium, which are: 0.01% to 5% of glucose, 0.01% to 5% of food grade calcium chloride, Food grade ferrous chloride 0.01% ~ 5%, food grade dipotassium hydrogen phosphate 0.01% ~ 5%.
所述步骤(4)中地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液的接种量以接入的种子液的质量占发酵培养基总质量百分比计,为1%~15%。The inoculum amount of Bacillus licheniformis HL-3 seed liquid in the step (4) is 1%-15% based on the weight of the inserted seed liquid in the total mass percentage of the fermentation medium.
与现有技术相比,本发明具有以下优点。Compared with the prior art, the present invention has the following advantages.
(1)整个制备过程没有高温处理,这不但可以更好地保留水产蛋白本身所含有的功能性成分的生物学活性,例如虾头和南极磷虾中的虾青素;而且还能更好地保留所制备的功能肽的生物学活性。本发明申请采用耐高温地衣芽孢杆菌发酵,在高温条件下可以抑制致病菌、腐败菌和其它杂菌的生长,因此本技术中培养基无需灭菌,这也是现有的采用常温菌种进行发酵法制备活性肽无法做到的。另外,本技术采用超滤膜去除酶解液中的蛋白酶,无需采用高温的方式进行灭酶。(1) There is no high-temperature treatment in the whole preparation process, which not only can better retain the biological activity of the functional components contained in the aquatic protein itself, such as astaxanthin in shrimp heads and Antarctic krill; The biological activity of the prepared functional peptide is retained. The application of the present invention uses high-temperature-resistant Bacillus licheniformis to ferment, which can inhibit the growth of pathogenic bacteria, spoilage bacteria and other miscellaneous bacteria under high-temperature conditions, so the culture medium in this technology does not need to be sterilized, which is also the existing normal-temperature bacteria. It is impossible to prepare active peptides by fermentation. In addition, this technology uses ultrafiltration membranes to remove proteases in the enzymatic hydrolysis solution, without the need to use high temperature methods to inactivate enzymes.
(2)简化了工序,降低了成本。由于本发明申请没有高温灭酶的过程,这不但降低了能耗,而且还会大大降低酶解液的美拉德反应,所以发酵液的颜色比较浅。而后续的膜分离又有一定的脱色效果,因此本技术中可以无需脱色这个程序,简化了工序,降低了成本。(2) The process is simplified and the cost is reduced. Because the application of the present invention does not have the process of high-temperature enzyme elimination, this not only reduces energy consumption, but also greatly reduces the Maillard reaction of the enzymolysis solution, so the color of the fermentation solution is relatively light. The subsequent membrane separation has a certain decolorization effect, so the decolorization procedure can be eliminated in this technology, which simplifies the process and reduces the cost.
(3)内源酶酶解与微生物发酵的完美结合。现有的发酵技术中,原料都需灭菌,这不但增加了能耗,而且又使得水产蛋白的内源酶失活。而本技术中原料无需灭菌,保留了水产蛋白中内源酶的活性。并且,微生物发酵的温度与内源酶的最适酶解温度一致,使得内源酶酶解与微生物发酵能完美结合在一起。正是由于本发明中充分利用内源酶的酶解作用,使得本发明无需另加蛋白酶。(3) The perfect combination of endogenous enzyme hydrolysis and microbial fermentation. In the existing fermentation technology, all raw materials need to be sterilized, which not only increases energy consumption, but also inactivates endogenous enzymes of aquatic proteins. However, in this technology, the raw materials do not need to be sterilized, and the activity of endogenous enzymes in the aquatic protein is retained. Moreover, the temperature of microbial fermentation is consistent with the optimum enzymolysis temperature of endogenous enzymes, so that endogenous enzyme enzymolysis and microbial fermentation can be perfectly combined. It is precisely because the enzymatic hydrolysis of endogenous enzymes is fully utilized in the present invention that no additional protease is needed in the present invention.
(4)制备成本不但要低于现有发酵技术,而且发酵效果也要优于现有的发酵技术。与现有的采用发酵法制备活性肽的技术相比,本发明申请原料无需灭绝,可降低能耗和成本。由于本发明申请提供的技术方案无需高温灭绝,保留了水产蛋白内源蛋白酶的酶活,这是现有的采用常温发酵菌种制备活性肽无法做到的,另外,在高温下酶的活性更强,因此,本技术采用耐高温菌种进行发酵,水产蛋白的水解度要高于现有的常温菌种发酵技术。(4) The preparation cost is not only lower than the existing fermentation technology, but also the fermentation effect is better than the existing fermentation technology. Compared with the existing technology of preparing active peptides by fermentation, the raw materials for the application of the present invention do not need to be extinct, which can reduce energy consumption and cost. Since the technical scheme provided by the application of the present invention does not require high-temperature extinction, the enzyme activity of the endogenous protease of the aquatic protein is retained, which is impossible to prepare active peptides by using normal temperature fermentation strains. In addition, the activity of the enzyme is higher at high temperature Strong, therefore, this technology uses high-temperature-resistant strains for fermentation, and the degree of hydrolysis of aquatic proteins is higher than that of the existing normal-temperature strain fermentation technology.
本发明提供了一种利用水产蛋白高温发酵制备活性肽的方法。本发明技术作用条件温和,更多地保留了制备的功能肽和水产蛋白本身所含功能性成分的生物学活性,并且简化了活性肽制备的工序和降低了活性肽的生产成本,有着良好的应用前景。The invention provides a method for preparing active peptides through high-temperature fermentation of aquatic proteins. The technology of the invention has mild action conditions, retains more of the biological activity of the prepared functional peptides and the functional components contained in the aquatic protein itself, simplifies the preparation process of the active peptides and reduces the production cost of the active peptides, and has good advantages Application prospects.
具体实施方式detailed description
为了更好地理解本发明,下面就水产蛋白的种类、发酵参数和发酵方式的选择结合实施例对本发明作进一步描述,但本发明的保护范围不限于此。In order to better understand the present invention, the following will further describe the present invention with regard to the selection of aquatic protein types, fermentation parameters and fermentation methods in conjunction with examples, but the protection scope of the present invention is not limited thereto.
实施例1:将斜面保藏的能产耐高温蛋白酶的地衣芽孢杆菌(Bacilluslicheniformis)HL-3接入到灭菌后冷却的LB液体培养基中,于55℃、150r/min培养12h,制备成地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液备用。将新鲜的南极磷虾绞碎后备用。将20公斤绞碎的南极磷虾和100公斤水加入到发酵罐中,并向发酵罐中加入300克葡萄糖、300克食品级氯化钙、300克食品级氯化亚铁和500克食品级磷酸氢二钾,获得发酵培养基;往发酵罐中的发酵培养基中加入8公斤地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液;发酵温度为55℃,无菌空气通入量为1.5vvm~2.5vvm,发酵罐的转速为250rpm~350rpm,发酵时间为42h;发酵结束后发酵液通过过滤去除沉淀得到上清液;上清液通过截留分子量为5000道尔顿的超滤膜的超滤去除大分子蛋白质而得到透过液;透过液然后通过截留分子量为200道尔顿的纳滤膜的纳滤去除氨基酸而得到浓缩液;浓缩液经过冷冻干燥而得到活性肽成品。Example 1: Inoculate Bacillus licheniformis HL-3, which is capable of producing thermostable protease, preserved on a slant into LB liquid medium cooled after sterilization, and cultivated at 55°C and 150r/min for 12h to prepare a lichen The seed liquid of Bacillus licheniformis HL-3 was reserved. Mince fresh Antarctic krill for later use. Add 20kg of minced Antarctic krill and 100kg of water to the fermenter and add 300g of glucose, 300g of food grade calcium chloride, 300g of food grade ferrous chloride and 500g of food grade Dipotassium hydrogen phosphate to obtain the fermentation medium; add 8 kg of Bacillus licheniformis HL-3 seed solution to the fermentation medium in the fermenter; the fermentation temperature is 55°C, and the sterile air intake is 1.5vvm~ 2.5vvm, the rotation speed of the fermenter is 250rpm-350rpm, and the fermentation time is 42h; after the fermentation, the fermentation liquid is filtered to remove the precipitate to obtain the supernatant; the supernatant is removed by ultrafiltration with an ultrafiltration membrane with a molecular weight cut-off of 5000 Daltons Macromolecular protein to obtain the permeate; the permeate is then filtered through a nanofiltration membrane with a molecular weight cut-off of 200 Daltons to remove amino acids to obtain a concentrate; the concentrate is freeze-dried to obtain the finished active peptide.
实施例2:将斜面保藏的能产耐高温蛋白酶的地衣芽孢杆菌(Bacilluslicheniformis)HL-3接入到灭菌后冷却的LB液体培养基中,于55℃、150r/min培养12h,制备成地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液备用。将新鲜的虾头绞碎后备用。将22公斤绞碎的虾头和100公斤水加入到发酵罐中,并向发酵罐中加入200克葡萄糖、400克食品级氯化钙、400克食品级氯化亚铁和600克食品级磷酸氢二钾,获得发酵培养基;往发酵罐中的发酵培养基中加入9公斤地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液;发酵温度为60℃,无菌空气通入量为1.5vvm~2.5vvm,发酵罐的转速为250rpm~350rpm,发酵时间为48h;发酵结束后发酵液通过过滤去除沉淀得到上清液;上清液通过截留分子量为5000道尔顿的超滤膜的超滤去除大分子蛋白质而得到透过液;透过液然后通过截留分子量为200道尔顿的纳滤膜的纳滤去除氨基酸而得到浓缩液;浓缩液经过冷冻干燥而得到活性肽成品。Example 2: Insert Bacillus licheniformis HL-3, which is capable of producing thermostable protease, preserved on a slant into LB liquid medium cooled after sterilization, and cultivated at 55°C and 150r/min for 12h to prepare a lichen The seed liquid of Bacillus licheniformis HL-3 was reserved. Mince fresh shrimp heads and set aside. Add 22 kg of minced shrimp heads and 100 kg of water to the fermenter, and add 200 g of glucose, 400 g of food grade calcium chloride, 400 g of food grade ferrous chloride and 600 g of food grade phosphoric acid into the fermenter dipotassium hydrogen to obtain the fermentation medium; add 9 kg of Bacillus licheniformis (Bacillus licheniformis) HL-3 seed solution to the fermentation medium in the fermenter; vvm, the rotation speed of the fermenter is 250rpm-350rpm, and the fermentation time is 48h; after the fermentation, the fermentation liquid is filtered to remove the precipitate to obtain the supernatant; Molecular protein to obtain the permeate; the permeate is then filtered through a nanofiltration membrane with a molecular weight cut-off of 200 Daltons to remove amino acids to obtain a concentrated solution; the concentrated solution is freeze-dried to obtain the finished active peptide.
实施例3:将斜面保藏的能产耐高温蛋白酶的地衣芽孢杆菌(Bacilluslicheniformis)HL-3接入到灭菌后冷却的LB液体培养基中,于55℃、150r/min培养12h,制备成地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液备用。将新鲜的罗非鱼下脚料绞碎后备用。将25公斤绞碎的罗非鱼下脚料和100公斤水加入到发酵罐中,并向发酵罐中加入450克葡萄糖、450克食品级氯化钙、350克食品级氯化亚铁和580克食品级磷酸氢二钾,获得发酵培养基;往发酵罐中的发酵培养基中加入10公斤地衣芽孢杆菌(Bacilluslicheniformis)HL-3种子液;发酵温度为57℃,无菌空气通入量为1.5vvm~2.5vvm,发酵罐的转速为250rpm~350rpm,发酵时间为45h;发酵结束后发酵液通过过滤去除沉淀得到上清液;上清液通过截留分子量为5000道尔顿的超滤膜的超滤去除大分子蛋白质而得到透过液;透过液然后通过截留分子量为200道尔顿的纳滤膜的纳滤去除氨基酸而得到浓缩液;浓缩液经过冷冻干燥而得到活性肽成品。Example 3: Insert the Bacillus licheniformis HL-3 capable of producing thermostable protease preserved on the slant into the LB liquid medium cooled after sterilization, and cultivate it at 55°C and 150r/min for 12h to prepare a lichen The seed liquid of Bacillus licheniformis HL-3 was reserved. The fresh tilapia leftovers are minced and set aside. 25 kg of minced tilapia scraps and 100 kg of water were added to the fermenter, and 450 g of glucose, 450 g of food grade calcium chloride, 350 g of food grade ferrous chloride and 580 g of Food grade dipotassium hydrogen phosphate to obtain fermentation medium; add 10 kg of Bacillus licheniformis HL-3 seed solution to the fermentation medium in the fermenter; the fermentation temperature is 57°C, and the sterile air intake is 1.5 vvm~2.5vvm, the rotation speed of the fermenter is 250rpm~350rpm, and the fermentation time is 45h; after the fermentation, the fermentation liquid is filtered to remove the precipitate to obtain the supernatant; The permeate is obtained by filtering out macromolecular proteins; the permeate is then filtered through a nanofiltration membrane with a molecular weight cut-off of 200 Daltons to remove amino acids to obtain a concentrate; the concentrate is freeze-dried to obtain a finished active peptide.
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