CN115466764A - Application of sodium chloride in improvement of bacillus subtilis to synthesis of bacitracin D, sodium chloride fermentation medium and method - Google Patents
Application of sodium chloride in improvement of bacillus subtilis to synthesis of bacitracin D, sodium chloride fermentation medium and method Download PDFInfo
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Abstract
Description
技术领域technical field
本发明属于微生物发酵技术领域,具体涉及氯化钠在提高枯草芽孢杆菌合成杆菌霉素D的应用和氯化钠发酵培养基及方法。The invention belongs to the technical field of microbial fermentation, and in particular relates to the application of sodium chloride in improving the synthesis of bacillus mycin D by Bacillus subtilis, a sodium chloride fermentation medium and a method.
背景技术Background technique
杆菌霉素D是由枯草芽孢杆菌中非核糖体肽合酶催化合成的一种属于iturin家族的抗菌脂肽,杆菌霉素D可以抑制黄曲霉和赭曲霉等农业病原真菌,因此,杆菌霉素D在保障粮食和食品安全以及防治真菌污染等方面非常重要。但是,现有技术中利用枯草芽孢杆菌在常规培养基进行发酵培养时杆菌霉素D的产量低。因此急需加强提高杆菌霉素D产量的研究。Bacitracin D is an antibacterial lipopeptide belonging to the iturin family synthesized by non-ribosomal peptide synthase in Bacillus subtilis. Bacitracin D can inhibit agricultural pathogenic fungi such as Aspergillus flavus and Ochra. Therefore, Bacitracin D is very important in ensuring food and food safety and preventing fungal contamination. However, in the prior art, when Bacillus subtilis is used for fermentation and culture in a conventional medium, the yield of bacinomycin D is low. Therefore, it is urgent to strengthen the research on increasing the production of bacitracin D.
发明内容Contents of the invention
有鉴于此,本发明的目的是提供一种能够有效提高枯草芽孢杆菌合成杆菌霉素D的方式。本发明提供了氯化钠在提高枯草芽孢杆菌合成杆菌霉素D的应用,在基础培养基中添加氯化钠后对枯草芽孢杆菌进行发酵培养生产杆菌霉素D,能够提高杆菌霉素D的产量。In view of this, the object of the present invention is to provide a method that can effectively improve the synthesis of bacillus mycin D by Bacillus subtilis. The invention provides the application of sodium chloride in improving the synthesis of bacillus mycin D by Bacillus subtilis, adding sodium chloride to the basal medium to ferment and cultivate the bacillus subtilis to produce bacillus mycin D, which can improve the production rate of bacillus mycin D Yield.
为了解决上述技术问题,本发明提出了以下技术方案:In order to solve the problems of the technologies described above, the present invention proposes the following technical solutions:
本发明提供了氯化钠在提高枯草芽孢杆菌合成杆菌霉素D的应用。The invention provides the application of sodium chloride in improving the synthesis of bacillus mycin D by bacillus subtilis.
本发明提供了一种氯化钠发酵培养基,所述氯化钠发酵培养基以水为溶剂,包含以下浓度的组分:酵母膏0.5~1.0g/L、L-谷氨酸2.0~5.0g/L、葡萄糖5.0~20.0g/L和氯化钠1.0~6.0g/L。The invention provides a sodium chloride fermentation medium. The sodium chloride fermentation medium uses water as a solvent and contains components at the following concentrations: 0.5-1.0 g/L of yeast extract, 2.0-5.0 g/L of L-glutamic acid g/L, glucose 5.0~20.0g/L and sodium chloride 1.0~6.0g/L.
优选的,所述氯化钠发酵培养基以水为溶剂,包含以下浓度的组分:酵母膏1.0g/L、L-谷氨酸5.0g/L、葡萄糖20.0g/L和氯化钠3.0g/L。Preferably, the sodium chloride fermentation medium uses water as a solvent and contains components of the following concentrations: yeast extract 1.0g/L, L-glutamic acid 5.0g/L, glucose 20.0g/L and sodium chloride 3.0 g/L.
本发明提供了一种提高杆菌霉素D产量的方法,其特征在于,包括以下步骤:采用上述技术方案所述氯化钠发酵培养基对枯草芽孢杆菌种子液进行发酵培养获得杆菌霉素D;所述发酵培养过程分批补料氯化钠发酵培养基。The invention provides a method for increasing the output of bacillus mycin D, which is characterized in that it comprises the following steps: using the sodium chloride fermentation medium described in the above technical solution to ferment and cultivate the Bacillus subtilis seed liquid to obtain the bacillus mycin D; The fermentation culture process is a fed-batch sodium chloride fermentation medium.
优选的,所述发酵培养为一次补料分批发酵培养;Preferably, the fermentation culture is a fed-batch fermentation culture;
所述一次补料分批发酵培养的条件包括:所述枯草芽孢杆菌种子液接种于氯化钠发酵培养基培养48~84h后补加1次新的氯化钠发酵培养基继续进行发酵培养后获得发酵液。The conditions for the one-time fed-batch fermentation culture include: the Bacillus subtilis seed liquid is inoculated in the sodium chloride fermentation medium and cultured for 48-84 hours, and then a new sodium chloride fermentation medium is added once to continue the fermentation culture. Obtain a fermented broth.
优选的,补加的氯化钠发酵培养基的体积为最初的氯化钠发酵培养基体积的30%~50%。Preferably, the volume of the added sodium chloride fermentation medium is 30% to 50% of the volume of the initial sodium chloride fermentation medium.
优选的,所述发酵培养的温度为30~37℃,转速为150~200r/min;所述发酵培养时间为139~171h。Preferably, the temperature of the fermentation culture is 30-37° C., the rotation speed is 150-200 r/min; the time of the fermentation culture is 139-171 h.
优选的,所述枯草芽孢杆菌的种子液的制备包括:枯草芽孢杆菌接种于种子培养基,于33~37℃培养至种子培养基的OD600为0.8~1.0获得枯草芽孢杆菌种子液。Preferably, the preparation of the Bacillus subtilis seed liquid comprises: inoculating the Bacillus subtilis on the seed medium, and culturing at 33-37° C. until the OD 600 of the seed medium is 0.8-1.0 to obtain the Bacillus subtilis seed liquid.
优选的,所述枯草芽孢杆菌种子液的接种量为氯化钠发酵培养基体积的3%~5%。Preferably, the inoculation amount of the Bacillus subtilis seed liquid is 3%-5% of the volume of the sodium chloride fermentation medium.
优选的,所述杆菌霉素D包括杆菌霉素DC14同系物、杆菌霉素DC15同系物和杆菌霉素DC16同系物中的一种或多种。Preferably, the bacitracin D includes one or more of bacitracin DC14 homologues, bacitracin DC15 homologues and bacitracin DC16 homologues.
本发明的有益效果:本发明提供了氯化钠在提高枯草芽孢杆菌合成杆菌霉素D的应用,本发明氯化钠能促进芽孢杆菌的杆菌霉素D合成酶基因表达,以此来提高杆菌霉素D的产量。实施例结果表明:应用本发明提供的氯化钠发酵培养基对枯草芽孢杆菌进行发酵培养获得的杆菌霉素D的产量明显提高,发酵液中杆菌霉素D的含量为478.79±13.41mg/L,枯草芽孢杆菌粗肽中的总杆菌霉素D的含量为17.34±0.41mg/g。Beneficial effects of the present invention: the present invention provides the application of sodium chloride in improving the synthesis of bacillus mycin D by Bacillus subtilis. Production of mycin D. The results of the examples show that the output of bacillus mycin D obtained by fermenting and culturing Bacillus subtilis by using the sodium chloride fermentation medium provided by the present invention is significantly improved, and the content of bacillus mycin D in the fermentation broth is 478.79±13.41mg/L , the content of total bacitracin D in the crude peptide of Bacillus subtilis was 17.34±0.41mg/g.
具体实施方式detailed description
本发明提供了氯化钠在提高枯草芽孢杆菌合成杆菌霉素D的应用。The invention provides the application of sodium chloride in improving the synthesis of bacillus mycin D by bacillus subtilis.
本发明提供了一种氯化钠发酵培养基,所述氯化钠发酵培养基以水为溶剂,包含以下浓度的组分:酵母膏0.5~1.0g/L、L-谷氨酸2.0~5.0g/L、葡萄糖5.0~20.0g/L和氯化钠1.0~6.0g/L。The invention provides a sodium chloride fermentation medium. The sodium chloride fermentation medium uses water as a solvent and contains components at the following concentrations: 0.5-1.0 g/L of yeast extract, 2.0-5.0 g/L of L-glutamic acid g/L, glucose 5.0~20.0g/L and sodium chloride 1.0~6.0g/L.
如无特殊说明,本发明对酵母膏、L-谷氨酸、葡萄糖和氯化钠的来源没有特殊限定,采用常规的市售产品即可。Unless otherwise specified, the present invention has no special limitation on the sources of yeast extract, L-glutamic acid, glucose and sodium chloride, and conventional commercially available products can be used.
在本发明中,所述氯化钠发酵培养基包括葡萄糖5.0~20.0g/L,优选为13.0~18.0g/L。在本发明实施例中,葡萄糖的添加量优选为20g/L或15.0g/L。In the present invention, the sodium chloride fermentation medium contains 5.0-20.0 g/L of glucose, preferably 13.0-18.0 g/L. In the embodiment of the present invention, the added amount of glucose is preferably 20 g/L or 15.0 g/L.
在本发明中,所述氯化钠发酵培养基包括酵母膏0.5~1.0g/L,优选为0.6~0.9g/L。在本发明实施例中酵母膏的添加量具体为1.0g/L或0.8g/L。本发明酵母膏可以为枯草芽孢杆菌的生长提供能量物质,促使枯草芽孢杆菌分泌更多的次级代谢产物。In the present invention, the sodium chloride fermentation medium includes 0.5-1.0 g/L of yeast extract, preferably 0.6-0.9 g/L. In the embodiment of the present invention, the amount of yeast extract added is specifically 1.0 g/L or 0.8 g/L. The yeast extract of the present invention can provide energy substances for the growth of the subtilis bacillus, and promote the subtilis bacillus to secrete more secondary metabolites.
在本发明中,所述氯化钠发酵培养基包括L-谷氨酸2.0~5.0g/L,优选为2.5~4.5g/L,更优选为4.0g/L。在本发明实施例中L-谷氨酸的添加量优选为5.0g/L。In the present invention, the sodium chloride fermentation medium includes 2.0-5.0 g/L of L-glutamic acid, preferably 2.5-4.5 g/L, more preferably 4.0 g/L. In the embodiment of the present invention, the added amount of L-glutamic acid is preferably 5.0 g/L.
在本发明中,所述氯化钠发酵培养基包括氯化钠1.0~6.0g/L,优选为2.0~5.0g/L,更优选为3.0g/L。In the present invention, the sodium chloride fermentation medium contains 1.0-6.0 g/L of sodium chloride, preferably 2.0-5.0 g/L, more preferably 3.0 g/L.
本发明优选所述氯化钠发酵培养基以水为溶剂,包含以下浓度的组分:酵母膏1.0g/L、L-谷氨酸5.0g/L、葡萄糖20.0g/L和氯化钠3.0g/L。In the present invention, the sodium chloride fermentation medium preferably uses water as a solvent, and comprises components of the following concentrations: yeast extract 1.0g/L, L-glutamic acid 5.0g/L, glucose 20.0g/L and sodium chloride 3.0 g/L.
本发明所述氯化钠发酵培养基中氯化钠、葡萄糖和L-谷氨酸均能促进杆菌霉素D合成酶基因表达进而有效提高枯草芽孢杆菌合成杆菌霉素D的产量。The sodium chloride, glucose and L-glutamic acid in the sodium chloride fermentation medium of the present invention can all promote the expression of the bacillus mycin D synthetase gene so as to effectively increase the yield of the bacillus mycin D synthesized by the bacillus subtilis.
本发明在酵母膏,L-谷氨酸和葡萄糖组成的基础培养基中添加氯化钠,并通过1次补料分批发酵发酵生产杆菌霉素D,使杆菌霉素D的产量提高,方法简单、易操作,解决了现有技术中枯草芽孢杆菌杆菌霉素D产量低的技术问题。In the present invention, sodium chloride is added to the basal medium composed of yeast extract, L-glutamic acid and glucose, and the production of bacillus mycin D is fermented by feeding batches once, so that the output of bacillus mycin D is improved, and the method The method is simple and easy to operate, and solves the technical problem of low yield of bacillus subtilis bacillus mycin D in the prior art.
本发明优选对氯化钠发酵培养基进行灭菌,所述灭菌温度优选为115℃、时间优选为20min。In the present invention, the sodium chloride fermentation medium is preferably sterilized, and the sterilization temperature is preferably 115° C., and the sterilization time is preferably 20 minutes.
本发明提供了一种提高杆菌霉素D产量的方法,包括以下步骤:采用上述技术方案所述氯化钠发酵培养基对枯草芽孢杆菌种子液进行发酵培养获得杆菌霉素D;所述发酵培养过程分批补料氯化钠发酵培养基。The invention provides a method for increasing the output of bacillus mycin D, comprising the following steps: using the sodium chloride fermentation medium described in the above technical scheme to ferment and cultivate the Bacillus subtilis seed liquid to obtain bacillus mycin D; Process fed-batch sodium chloride fermentation medium.
在本发明中,所述枯草芽孢杆菌种子液的制备优选包括:枯草芽孢杆菌接种于种子培养基,于33~37℃培养至种子培养基的OD600为0.8~1.0获得枯草芽孢杆菌种子液。In the present invention, the preparation of the Bacillus subtilis seed solution preferably includes: inoculating the Bacillus subtilis on the seed medium, culturing at 33-37° C. until the OD 600 of the seed medium is 0.8-1.0 to obtain the Bacillus subtilis seed solution.
接种于种子培养基前,本发明优选将斜面保藏的枯草芽孢杆菌接种于种子培养基培养后获得枯草芽孢杆菌种子液。在本发明中,所述种子培养基温度优选为33~37℃,进一步优选为34~36℃,更优选为35℃,在本发明实施例中所述种子培养的温度优选为37℃;本发明优选培养至枯草芽孢杆菌种子液OD600为0.8~1.0,进一步优选为0.85~0.95,更优选为0.9。本发明实施例中优选培养至枯草芽孢杆菌种子液OD600为0.8。本发明所述种子培养优选为恒温培养。Before being inoculated in the seed medium, the present invention preferably inoculates the Bacillus subtilis preserved on the slant into the seed medium and cultivates it to obtain the Bacillus subtilis seed liquid. In the present invention, the temperature of the seed culture medium is preferably 33-37°C, more preferably 34-36°C, more preferably 35°C, and the temperature of the seed culture in the embodiment of the present invention is preferably 37°C; In the present invention, it is preferred to cultivate until the OD 600 of the Bacillus subtilis seed solution is 0.8-1.0, more preferably 0.85-0.95, and more preferably 0.9. In the embodiment of the present invention, it is preferred to cultivate until the OD 600 of the Bacillus subtilis seed solution is 0.8. The seed cultivation in the present invention is preferably constant temperature cultivation.
本发明对所述枯草芽孢杆菌种子液进行发酵培养获得杆菌霉素D;所述发酵培养过程分批补料氯化钠发酵培养基。In the present invention, the bacillus subtilis seed liquid is fermented and cultured to obtain bacillus mycin D; the fermentation culture process is fed with sodium chloride fermentation medium in batches.
本发明利用氯化钠发酵培养基对枯草芽孢杆菌种子液进行发酵培养获得杆菌霉素D;所述发酵培养过程分批补料氯化钠发酵培养基。The present invention uses the sodium chloride fermentation medium to ferment and cultivate the Bacillus subtilis seed liquid to obtain the bacillus mycin D; the fermentation and cultivation process feeds the sodium chloride fermentation medium in batches.
本发明优选将枯草芽孢杆菌种子液接种于氯化钠发酵培养基进行发酵培养。本发明优选按照体积比3%~5%的比例将枯草芽孢杆菌种子液接种于氯化钠发酵培养基,进一步优选为3.5%~4.5%,更优选为4%。在本发明实施例中,枯草芽孢杆菌种子液接种于氯化钠发酵培养基接种量为体积比5%。In the present invention, it is preferred to inoculate the Bacillus subtilis seed solution in a sodium chloride fermentation medium for fermentation culture. In the present invention, the Bacillus subtilis seed liquid is preferably inoculated in the sodium chloride fermentation medium according to the volume ratio of 3%-5%, more preferably 3.5%-4.5%, more preferably 4%. In the embodiment of the present invention, the inoculation amount of the Bacillus subtilis seed solution inoculated into the sodium chloride fermentation medium is 5% by volume.
在本发明中,所述发酵培养的转速优选为150~200r/min,进一步优选为165~195r/min,更优选为180r/min。本发明所述发酵培养的温度为30~37℃,进一步优选为31~34℃,更优选为33℃。在本发明中,所述发酵培养的时间优选为139~171h,进一步优选为143~156h,更优选为147h。在本发明中,所述发酵培养过程分批补料氯化钠发酵培养基;本发明所述发酵培养的时间为总的培养时间,包括补加氯化钠培养基之前的发酵培养总时间和补加氯化钠培养基之后的发酵培养总时间。In the present invention, the rotational speed of the fermentation culture is preferably 150-200 r/min, more preferably 165-195 r/min, more preferably 180 r/min. The temperature of the fermentation culture in the present invention is 30-37°C, more preferably 31-34°C, more preferably 33°C. In the present invention, the fermentation culture time is preferably 139-171 h, more preferably 143-156 h, more preferably 147 h. In the present invention, described fermentation culture process feeds sodium chloride fermentation culture medium in batches; The time of fermentation culture described in the present invention is total culture time, comprises the total time of fermentation culture before adding sodium chloride culture medium and The total time of fermentation culture after supplementing the sodium chloride medium.
在本发明中,所述发酵培养优选为一次补料分批发酵培养。本发明所述一次补料分批发酵培养的条件优选包括:所述枯草芽孢杆菌种子液接种于氯化钠发酵培养基培养48~84h后补加1次新的氯化钠发酵培养基继续进行发酵培养后获得发酵液。In the present invention, the fermentation culture is preferably a fed-batch fermentation culture. The conditions of the one-time fed-batch fermentation culture of the present invention preferably include: the Bacillus subtilis seed liquid is inoculated in a sodium chloride fermentation medium for 48-84 hours, and then a new sodium chloride fermentation medium is added to continue Fermentation broth is obtained after fermentation.
本发明所述补加氯化钠培养基之前的发酵培养时间优选为48~84h,进一步优选为54~72h,更优选为63h。在本发明实施例中,所述补料分批发酵的条件优选为:将枯草芽孢杆菌种子液接入最初的氯化钠发酵培养基中发酵培养至63h,向发酵液中补加新的氯化钠发酵培养基后发酵培养84h,发酵培养至147h获得枯草芽孢杆菌发酵液。The fermentation culture time before adding the sodium chloride medium in the present invention is preferably 48-84 hours, more preferably 54-72 hours, more preferably 63 hours. In the embodiment of the present invention, the conditions of the fed-batch fermentation are preferably as follows: the Bacillus subtilis seed liquid is inserted into the initial sodium chloride fermentation medium for fermentation and cultivation for 63 hours, and new chlorine is added to the fermentation liquid. The sodium chloride fermentation medium was post-fermented for 84 hours, and fermented for 147 hours to obtain a Bacillus subtilis fermentation broth.
在本发明中,补加的新的氯化钠发酵培养基的体积优选为最初的氯化钠发酵培养基体积的30%~50%,进一步优选为35%~45%,更优选为40%。在本发明实施例中,补加的新的氯化钠发酵培养基的体积优选为最初的氯化钠发酵培养基体积的50%,本发明补加的新的氯化钠发酵培养基的体积为最初的氯化钠发酵培养基体积的50%是为了提高枯草芽孢杆菌发酵生产杆菌霉素D的产量。In the present invention, the volume of the new sodium chloride fermentation medium added is preferably 30% to 50% of the volume of the initial sodium chloride fermentation medium, more preferably 35% to 45%, more preferably 40% . In an embodiment of the present invention, the volume of the new sodium chloride fermentation medium added is preferably 50% of the initial sodium chloride fermentation medium volume, and the volume of the new sodium chloride fermentation medium added by the present invention 50% of the volume of the initial sodium chloride fermentation medium is to increase the yield of bacinomycin D produced by fermentation of Bacillus subtilis.
在本发明中,所述斜面保藏培养基组分优选包括3.0g/L牛肉浸膏,10g/L胰蛋白胨,5g/L氯化钠,15g/L琼脂和水1L。In the present invention, the components of the slant preservation medium preferably include 3.0 g/L beef extract, 10 g/L tryptone, 5 g/L sodium chloride, 15 g/L agar and 1 L of water.
所述种子培养基优选包括3.0g/L牛肉浸膏、10g/L胰蛋白胨、5g/L氯化钠和水1L。所述氯化钠发酵培养基在上文已经论述,在此不再赘述。The seed medium preferably includes 3.0 g/L beef extract, 10 g/L tryptone, 5 g/L sodium chloride and 1 L of water. The sodium chloride fermentation medium has been discussed above and will not be repeated here.
获得枯草芽孢杆菌发酵液后,本发明优选对枯草芽孢杆菌发酵液依次进行第一次离心、酸沉、第二次离心、萃取和第三次离心获得杆菌霉素D。本发明将枯草芽孢杆菌发酵液进行第一次离心,获得上清液后,本发明优选对上清液进行酸沉浸提和第二次离心获得杆菌霉素D粗肽。本发明所述酸沉优选利用HCl将上清液的pH值调至2.0以下,室温静置4h获得酸沉后的上清液进行第二次离心。本发明所述第一次离心的转速优选为5500~6500r/min,进一步优选为5900~6100r/min,更优选为6000r/min。本发明所述第二次离心的转速与第一次离心的转速相同。本发明所述第一次离心的时间优选为10~20min,进一步优选为13~18min,更优选为15min,第二次离心时间优选为10min。After the Bacillus subtilis fermentation liquid is obtained, the present invention preferably performs the first centrifugation, acid precipitation, second centrifugation, extraction and third centrifugation on the Bacillus subtilis fermentation liquid in order to obtain the bacillus mycin D. In the present invention, the Bacillus subtilis fermentation liquid is centrifuged for the first time to obtain the supernatant, and the supernatant is preferably subjected to acid immersion extraction and second centrifugation to obtain the crude bacillus mycin D peptide. The acid precipitation in the present invention preferably uses HCl to adjust the pH value of the supernatant to below 2.0, and leave it at room temperature for 4 hours to obtain the supernatant after acid precipitation for the second centrifugation. The rotating speed of the first centrifugation in the present invention is preferably 5500-6500r/min, more preferably 5900-6100r/min, and more preferably 6000r/min. The rotation speed of the second centrifugation in the present invention is the same as that of the first centrifugation. The time of the first centrifugation in the present invention is preferably 10-20 min, more preferably 13-18 min, more preferably 15 min, and the second centrifugation time is preferably 10 min.
获得杆菌霉素D粗肽沉淀后,本发明优选对获得的杆菌霉素D粗肽沉淀进行萃取和第三次离心,获得萃取上清液。在本发明中,本发明所述萃取的时间为70~80min,更优选为72min;所述萃取用萃取剂优选为甲醇,所述杆菌霉素D粗肽沉淀与甲醇的用量比优选为0.1~0.5g:0.5~2.0mL,进一步优选为0.3~0.5g:1.5mL,更优选为0.4g:1.5mL。在本发明中,所述第三次离心的转速优选为8000~12000r/min,进一步优选为9500~10500r/min,更优选为10000r/min,离心时间优选为7~11min,进一步优选为9~10.5min,更优选为10min。本发明甲醇可以有效萃取杆菌霉素D。After obtaining the bacitracin D crude peptide precipitate, the present invention preferably extracts and centrifuges the obtained bacitracin D crude peptide precipitate to obtain an extraction supernatant. In the present invention, the extraction time of the present invention is 70 to 80 minutes, more preferably 72 minutes; the extraction agent for the extraction is preferably methanol, and the ratio of the amount of the bacitracin D crude peptide precipitation to methanol is preferably 0.1 to 80 minutes. 0.5g: 0.5-2.0mL, more preferably 0.3-0.5g: 1.5mL, more preferably 0.4g: 1.5mL. In the present invention, the rotational speed of the third centrifugation is preferably 8000-12000r/min, more preferably 9500-10500r/min, more preferably 10000r/min, and the centrifugation time is preferably 7-11min, more preferably 9-10min. 10.5 min, more preferably 10 min. The methanol of the present invention can effectively extract the bacillus mycin D.
获得萃取上清液后,本发明优选采用高效液相色谱(HPLC)法对萃取上清液中的杆菌霉素D及其同系物的含量进行测定。本发明所述杆菌霉素D包括杆菌霉素DC14同系物、杆菌霉素DC15同系物和杆菌霉素DC16同系物中的一种或多种。在本发明中,所述杆菌霉素DC14同系物为十四碳β-氨基脂肪酸环七肽(C14-β-NH2COOH-Asn-Tyr-Asn-ProGlu-Ser-Thr);所述杆菌霉素DC15同系物为十五碳β-氨基脂肪酸环七肽(C15-β-NH2COOH-Asn-Tyr-Asn-ProGlu-Ser-Thr);所述杆菌霉素DC16同系物为十六碳β-氨基脂肪酸环七肽(C16-β-NH2COOH-Asn-Tyr-Asn-ProGlu-Ser-Thr)。利用本发明的技术方案枯草芽孢杆菌发酵生产杆菌霉素D的总产量、杆菌霉素DC14同系物产量、杆菌霉素DC15同系物产量和杆菌霉素DC16同系物产量均提高。After the extraction supernatant is obtained, the present invention preferably uses a high performance liquid chromatography (HPLC) method to measure the content of the bacitracin D and its homologues in the extraction supernatant. The bacillus mycin D in the present invention includes one or more of the bacillus mycin DC14 homologue, the bacillus mycin DC15 homologue and the bacillus mycin DC16 homologue. In the present invention, the bacillus mycin DC14 homologue is fourteen carbon β-amino fatty acid ring heptapeptide (C 14 -β-NH 2 COOH-Asn-Tyr-Asn-ProGlu-Ser-Thr); the bacillus The DC15 homolog of bacitramycin is 15-carbon β-amino fatty acid ring heptapeptide (C 15 -β-NH 2 COOH-Asn-Tyr-Asn-ProGlu-Ser-Thr); the homolog of bacitramycin DC16 is 16 Carbon β-amino fatty acid cyclic heptapeptide (C 16 -β-NH 2 COOH-Asn-Tyr-Asn-ProGlu-Ser-Thr). The total yield of bacillus mycin D, the yield of bacillus mycin DC14 homologue, the yield of bacillus mycin DC15 homologue and the yield of bacillus mycin DC16 homologue are all increased by using the technical solution of the invention.
金属盐可以激活生物合成途径中某些基因和酶来提高目标代谢产物的合成能力。本发明创新性的将氯化钠添加在基础培养基中,制备氯化钠发酵培养基,并采用补料分批发酵生产杆菌霉素D,解决了现有技术中杆菌霉素D的产量低的技术问题,为实现杆菌霉素D大规模的工业化生产奠定技术支撑。Metal salts can activate certain genes and enzymes in the biosynthetic pathway to improve the synthesis ability of target metabolites. The present invention innovatively adds sodium chloride into the basal medium to prepare a sodium chloride fermentation medium, and adopts fed-batch fermentation to produce bacillusmycin D, which solves the low yield of bacillusmycin D in the prior art technical problems, laying technical support for the large-scale industrial production of bacillus mycin D.
为了进一步说明本发明,下面结合实施例对本发明提供的技术方案进行详细地描述,但不能将它们理解为对本发明保护范围的限定。In order to further illustrate the present invention, the technical solutions provided by the present invention will be described in detail below in conjunction with examples, but they should not be construed as limiting the protection scope of the present invention.
实施例1Example 1
1培养基1 medium
氯化钠发酵培养基组分:酵母膏1.0g/L、L-谷氨酸5.0g/L、葡萄糖20.0g/L、氯化钠3g/L和1L水。Sodium chloride fermentation medium components: yeast extract 1.0g/L, L-glutamic acid 5.0g/L, glucose 20.0g/L, sodium chloride 3g/L and 1L water.
斜面保藏培养基组分:牛肉浸膏3.0g/L、胰蛋白胨10g/L、氯化钠5g/L、琼脂15g/L和1L水。Slant preservation medium components: beef extract 3.0g/L, tryptone 10g/L, sodium chloride 5g/L, agar 15g/L and 1L water.
种子培养基组分:牛肉浸膏3.0g/L,胰蛋白胨10g/L、氯化钠5g/L和1L水。Seed medium components: beef extract 3.0g/L, tryptone 10g/L, sodium chloride 5g/L and 1L water.
2补料分批发酵培养2-fed-batch fermentation culture
(1)挑取斜面保藏的枯草芽孢杆菌接入种子培养基,在温度为37℃的条件下恒温培养至枯草芽孢杆菌种子液OD600为0.8即可,获得枯草芽孢杆菌种子液。(1) Pick the Bacillus subtilis preserved on the slant and insert it into the seed medium, and culture it at a constant temperature at 37° C. until the OD 600 of the Bacillus subtilis seed solution is 0.8 to obtain the Bacillus subtilis seed solution.
(2)将步骤(1)的枯草芽孢杆菌种子液接种于氯化钠发酵培养基进行补料分批发酵培养。以接种完成开始计时:氯化钠发酵培养基的体积为300mL,枯草芽孢杆菌种子液的体积为15mL,枯草芽孢杆菌种子液的接种体积为氯化钠发酵培养基体积的5%,接种后在温度为33℃,转速为180r/min的条件下进行发酵培养至63h,向发酵液中添加1次新鲜的氯化钠发酵培养基125mL,于温度为33℃,180r/min的条件下继续发酵培养至147h,获得枯草芽孢杆菌补料分批发酵培养发酵液。补料分批发酵培养总时间为147h。(2) inoculating the Bacillus subtilis seed solution in step (1) into a sodium chloride fermentation medium to carry out fed-batch fermentation culture. Start timing with the completion of inoculation: the volume of the sodium chloride fermentation medium is 300mL, the volume of the Bacillus subtilis seed solution is 15mL, and the inoculation volume of the Bacillus subtilis seed solution is 5% of the volume of the sodium chloride fermentation medium. The temperature is 33°C, and the rotation speed is 180r/min, and the fermentation is carried out for 63 hours, and 125mL of fresh sodium chloride fermentation medium is added to the fermentation liquid once, and the temperature is 33°C, and the fermentation is continued under the conditions of 180r/min After culturing for 147 hours, the Bacillus subtilis fed-batch fermentation culture broth was obtained. The total time of fed-batch fermentation was 147h.
取40.0mL枯草芽孢杆菌发酵液于6000r/min的条件下离心15min,弃菌体,取上清液,用HCl将上清液pH调至2.0以下,室温静置4h,再次在6000r/min的条件下离心10min,得到杆菌霉素D粗肽沉淀,在沉淀0.4g中加入1.5mL甲醇进行萃取,萃取时间为72min,10000r/min离心10min,取上清液,采用高效液相色谱(HPLC)法对上清液中的杆菌霉素D及其同系物的含量进行测定。Take 40.0mL of Bacillus subtilis fermentation broth and centrifuge at 6000r/min for 15min, discard the bacteria, take the supernatant, adjust the pH of the supernatant to below 2.0 with HCl, let it stand at room temperature for 4h, and again at 6000r/min Centrifuge for 10 min under the conditions to obtain the precipitate of crude bacitracin D peptide, add 1.5 mL of methanol to 0.4 g of the precipitate for extraction, the extraction time is 72 min, centrifuge at 10000 r/min for 10 min, take the supernatant, and use high-performance liquid chromatography (HPLC) The content of bacitracin D and its homologues in the supernatant was determined by this method.
该补料分批发酵培养实验共设置5个平行实验。A total of 5 parallel experiments were set up in this fed-batch fermentation experiment.
实施例2Example 2
发酵培养基中添加氯化钠,氯化钠的添加量为1.0g/L,其余条件同实施例1。Sodium chloride was added in the fermentation medium, and the addition amount of sodium chloride was 1.0g/L, and all the other conditions were the same as in Example 1.
实施例3Example 3
发酵培养基中添加氯化钠,氯化钠的添加量为6.0g/L,其余条件同实施例1。Sodium chloride was added in the fermentation medium, and the addition amount of sodium chloride was 6.0g/L, and all the other conditions were the same as in Example 1.
对比例1Comparative example 1
不进行补料,其余条件同实施例1。Feeding is not carried out, and all the other conditions are the same as in Example 1.
对比例2Comparative example 2
发酵培养基中不添加氯化钠,其余条件同实施例1。Sodium chloride is not added in the fermentation medium, and all the other conditions are the same as in Example 1.
对比例3Comparative example 3
发酵培养基中以碳酸钠替换氯化钠,其余条件同实施例1。Sodium chloride was replaced with sodium carbonate in the fermentation medium, and all the other conditions were the same as in Example 1.
对比例4Comparative example 4
发酵培养基中添加氯化钠,氯化钠的添加量为0.5g/L,其余条件同实施例1。Sodium chloride was added in the fermentation medium, and the addition amount of sodium chloride was 0.5g/L, and all the other conditions were the same as in Example 1.
对比例5Comparative example 5
发酵培养基中添加氯化钠,氯化钠的添加量为8g/L,其余条件同实施例1。Sodium chloride was added in the fermentation medium, and the addition amount of sodium chloride was 8g/L, and all the other conditions were the same as in Example 1.
对实施例1~3和对比例1~5获得的枯草芽孢杆菌发酵液中的杆菌霉素D及其同系物的含量进行测定,测定方法采用高效液相色谱(HPLC)法。具体HPLC条件和测定方法参照现有技术(Qian Shiquan,Lu Hedong,Meng Panpan,Zhang Chong,Lv Fengxia,BieXiaomei,Lu Zhaoxin,Effect of inulin on efficient production and regulatorybiosynthesis ofbacillomycin D in Bacillus subtilis fmbJ,BioresourceTechnology,2015,179:260-267.)进行。实施例1~3和对比例1~5的5次平行实验的测定结果的平均值见表1。The content of the bacillus mycin D and its homologues in the Bacillus subtilis fermentation liquid obtained in Examples 1-3 and Comparative Examples 1-5 were determined, and the determination method adopted a high performance liquid chromatography (HPLC) method. Specific HPLC conditions and assay methods refer to prior art (Qian Shiquan, Lu Hedong, Meng Panpan, Zhang Chong, Lv Fengxia, BieXiaomei, Lu Zhaoxin, Effect of inulin on efficient production and regulatory biosynthesis of bacillomycin D in Bacillus subtilis fmbJ, BioresourceTechnology, 2015, 179:260-267.) proceed. See Table 1 for the average values of the measurement results of 5 parallel experiments in Examples 1-3 and Comparative Examples 1-5.
表1实施例1~3和对比例1~5获得的枯草芽孢杆菌发酵液中的杆菌霉素D及其同系物的含量(mg/L)和粗肽中杆菌霉素D含量(mg/g)Table 1 The content (mg/L) of bacitracin D and its homologs in the Bacillus subtilis fermentation broth obtained in Table 1 Examples 1-3 and Comparative Examples 1-5 and the content (mg/g) of bacitracin D in the crude peptide )
根据表1可知,本发明以氯化钠发酵培养基为基料进行1次补料发酵,有效提高了枯草芽孢杆菌的杆菌霉素D产量。According to Table 1, it can be known that the present invention uses the sodium chloride fermentation medium as the base material to carry out 1 fed-batch fermentation, which effectively improves the bacillus mycin D output of Bacillus subtilis.
尽管上述实施例对本发明做出了详尽的描述,但它仅仅是本发明一部分实施例,而不是全部实施例,人们还可以根据本实施例在不经创造性前提下获得其他实施例,这些实施例都属于本发明保护范围。Although the above-mentioned embodiment has described the present invention in detail, it is only a part of the embodiments of the present invention, rather than all embodiments. People can also obtain other embodiments according to the present embodiment without inventive step. These embodiments All belong to the protection scope of the present invention.
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钱时权: "Bacillomycin D的高效合成调控及赫曲霉污染控制研究", 中国博士学位论文全文数据库工程科技I辑, pages 67 - 68 * |
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