CN108004256A - Glucose oxidase gene Glox, albumen, pichia pastoris yeast and its preparation and application - Google Patents
Glucose oxidase gene Glox, albumen, pichia pastoris yeast and its preparation and application Download PDFInfo
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Abstract
本发明属于新基因的制备及工程菌的构建,特别是指一种葡萄糖氧化酶基因Glox及巴斯德毕赤酵母的制备、构建和应用。是以5¢端ATGAAGCTCCTTGGCCTCC和3¢端CTAATTAACAGTAGCGTTGTAATC为特异引物,以扩展青霉DNA为模板,采用PCR扩增方法获得葡萄糖氧化酶基因Glox,并成功构建了巴斯德毕赤酵母工程菌。本发明解决了目前重组葡萄糖氧化酶基因进行异源表达的问题,利用本发明获得了全长的Glox基因及其构建的穿梭表达载体,进一步转化到毕赤酵母X33菌株,经筛选鉴定得到一株较原始菌株较高分泌表达葡萄糖氧化酶的菌株。本发明方法简单易行,成本低廉,这为葡萄糖氧化酶大规模生产奠定了良好的基础。
The invention belongs to the preparation of new genes and the construction of engineering bacteria, in particular to the preparation, construction and application of a glucose oxidase gene Glox and Pichia pastoris. Using the 5¢end ATGAAGCTCCTTGGCCTCC and the 3¢end CTAATTAACAGTAGCGTTGTAATC as specific primers, using Penicillium elongatus DNA as a template, the glucose oxidase gene Glox was obtained by PCR amplification method, and the engineering strain of Pichia pastoris was successfully constructed. The present invention solves the problem of heterologous expression of recombinant glucose oxidase gene at present, obtains the full-length Glox gene and its constructed shuttle expression vector by using the present invention, further transforms into Pichia pastoris X33 strain, and obtains a strain through screening and identification The strain expressing glucose oxidase had a higher secretion than the original strain. The method of the invention is simple and easy, and the cost is low, which lays a good foundation for the large-scale production of glucose oxidase.
Description
技术领域technical field
本发明属于新基因的制备及工程菌的构建,特别是指一种葡萄糖氧化酶基因Glox、蛋白、巴斯德毕赤酵母及其制备和应用。The invention belongs to the preparation of new genes and the construction of engineering bacteria, in particular to a glucose oxidase gene Glox, protein, Pichia pastoris and its preparation and application.
背景技术Background technique
葡萄糖氧化酶是一种需氧脱氢酶,能够专一的催化β-D-葡萄糖生成葡萄糖酸和过氧化氢。葡萄糖氧化酶的催化特性使其具有去葡萄糖、脱氧、杀菌等功能,且安全无毒无副作用,是国家允许使用的酶制剂之一,在食品的加工保鲜、医学等方面都有广泛的应用。Glucose oxidase is an aerobic dehydrogenase that can specifically catalyze β-D-glucose to generate gluconic acid and hydrogen peroxide. The catalytic properties of glucose oxidase enable it to remove glucose, deoxidize, sterilize and other functions, and it is safe, non-toxic and without side effects.
葡萄糖氧化酶广泛分布于动植物、微生物体内。由于霉菌产酶能力强,目前用于研究和工业化菌种主要有黑曲霉和青霉属菌株,但霉菌发酵生产葡萄糖氧化酶过程中,过氧化氢酶、纤维素酶及淀粉酶等大量杂酶的存在给纯化带来相当的困难。扩展青霉属于青霉的一种,同样存在这样的问题。近几年市场对葡萄糖氧化酶的需求量逐年增长,对质量要求也逐年提高。所以我国葡萄糖氧化酶技术水平所存在的产量低、酶活低、提纯繁琐、酶活检测方法操作复杂等问题亟待解决。Glucose oxidase is widely distributed in animals, plants and microorganisms. Due to the strong ability of mold to produce enzymes, the currently used research and industrial strains mainly include Aspergillus niger and Penicillium strains. The presence of the purification brings considerable difficulties. Penicillium extensa belongs to a kind of Penicillium, which also has such problems. In recent years, the market demand for glucose oxidase has increased year by year, and the quality requirements have also increased year by year. Therefore, the problems of low yield, low enzyme activity, cumbersome purification, and complicated operation of enzyme activity detection methods in the technical level of glucose oxidase in my country need to be solved urgently.
重组葡萄糖氧化酶基因进行异源表达可有效地解决这些问题。尤其是毕赤酵母表达外源蛋白具有表达量高、稳定性好、培养成本低和产物易分离纯化等优点,适于大体积高密度连续发酵,具有强且易控的醇氧化酶(Alcohol oxidase,AOX)启动子等优点,可严格控制外源基因的表达。Heterologous expression of recombinant glucose oxidase gene can effectively solve these problems. In particular, the expression of exogenous proteins by Pichia pastoris has the advantages of high expression, good stability, low culture cost, and easy separation and purification of products. , AOX) promoter and other advantages, can strictly control the expression of foreign genes.
通过基因工程手段改造葡萄糖氧化酶生产菌株,获得萄糖氧化酶准确高效的生产和提取方法,提高产酶量,为后期的工业化生产提供了导向基础,提高其经济效益。Through the transformation of glucose oxidase production strains by means of genetic engineering, the accurate and efficient production and extraction methods of glucose oxidase can be obtained, and the enzyme production can be increased, which provides a guiding basis for later industrial production and improves its economic benefits.
申请人在申请号为201510893562.8的发明专利申请中公开了一种葡萄糖氧化酶基因GOD、利用其编码的蛋白以及转化的毕赤酵母基因工程菌。葡萄糖氧化酶基因GOD是以5′端ATGAAGTCCACTATTATCACCTCCA和3′端CTAGGCACTTTT GGCATAGTCTTCA为特异引物,以点青霉DNA为模板,采用PCR扩增方法获得。获得了全长的GOD基因及其构建的穿梭表达载体,进一步转化到毕赤酵母基因工程菌,经筛选鉴定得到一株较原始菌株较高分泌表达葡萄糖氧化酶的菌株,所获得的转基因毕赤酵母工程菌,在10L发酵罐水平检测条件下,甲醇诱导144小时,发酵液中的酶活达到594U/ml,显著提高了发酵酶活;并且通过基因工程手段改造葡萄糖氧化酶生产菌株,还可以获得萄糖氧化酶准确高效的生产,提高产酶量(9g/L)。上述现有技术存在的问题是GOD的大规模生产广泛采用黑曲霉或青霉菌发酵,但黑曲霉和青霉菌发酵生产GOD过程中,过氧化氢酶、纤维素酶及淀粉酶等大量杂蛋白的存在给纯化带来相当大的困难。因此,通过构建工程菌实现葡萄糖氧化酶的异源高效表达,研制及生产高品质的GOD制剂,是一条比较经济有效的途径。In the invention patent application with application number 201510893562.8, the applicant disclosed a glucose oxidase gene GOD, a protein encoded by it, and a transformed genetically engineered strain of Pichia pastoris. Glucose oxidase gene GOD was obtained by PCR amplification method using 5' end ATGAAGTCCACTATTATCACCTCCA and 3' end CTAGGCACTTTTT GGCATAGTCTTCA as specific primers and Penicillium pointis DNA as template. The full-length GOD gene and its constructed shuttle expression vector were obtained, and further transformed into Pichia pastoris genetically engineered bacteria. After screening and identification, a strain with higher secretion and expression of glucose oxidase than the original strain was obtained. The obtained transgenic Pichia Yeast engineered bacteria, under the detection condition of 10L fermenter level, induced by methanol for 144 hours, the enzyme activity in the fermentation broth reached 594U/ml, which significantly improved the fermentation enzyme activity; and the glucose oxidase production strain was modified by genetic engineering means, and it can also Accurate and efficient production of glucose oxidase is obtained, and the amount of enzyme production (9g/L) is increased. The problem that the above-mentioned prior art exists is that the large-scale production of GOD adopts Aspergillus niger or Penicillium fermentation widely, but in the process of producing GOD by Aspergillus niger and Penicillium fermentation, the production of a large amount of miscellaneous proteins such as catalase, cellulase and amylase Presence poses considerable difficulties for purification. Therefore, it is a more economical and effective way to develop and produce high-quality GOD preparations through the construction of engineered bacteria to realize the heterologous and efficient expression of glucose oxidase.
申请人检索的对比文件包括:The comparative documents searched by the applicant include:
1、申请号为CN105936910A的专利文献中出发菌株为黑曲霉的GOD做的异源表达,但其酶活表达水平仅为77U/ml。另外其做了突变,氨基酸序列有改变,我们仅对基因序列做了改变,但氨基酸序列与原始出发菌株扩展青霉的一致。其毕赤酵母为重组毕赤酵母GS115,我们用的是X33。1. In the patent document with application number CN105936910A, the starting strain is the heterologous expression of GOD of Aspergillus niger, but the enzyme activity expression level is only 77U/ml. In addition, it was mutated and the amino acid sequence was changed. We only changed the gene sequence, but the amino acid sequence was consistent with that of the original starting strain of Penicillium expansica. The Pichia pastoris is recombinant Pichia pastoris GS115, and we use X33.
2、申请号为CN106591249A的专利文献中所用的菌株为黑曲霉,对黑曲霉的发酵工艺做了优化,但霉菌发酵生产葡萄糖氧化酶过程中,过氧化氢酶、纤维素酶及淀粉酶等大量杂酶的存在给纯化带来相当的困难。2. The strain used in the patent literature with application number CN106591249A is Aspergillus niger, and the fermentation process of Aspergillus niger has been optimized, but in the process of producing glucose oxidase by mold fermentation, a large amount of catalase, cellulase and amylase, etc. The presence of hybrid enzymes brings considerable difficulties to purification.
3、申请号为CN105950577A的专利文献中对CN105936910A的提升,对上面序列做了突变,使得酶热稳定性有所提高。并未提及发酵酶活。3. The improvement of CN105936910A in the patent document with the application number CN105950577A, the above sequence is mutated, which improves the thermal stability of the enzyme. Fermentative enzyme activity is not mentioned.
发明内容Contents of the invention
本发明的目的之一在于提供一种葡萄糖氧化酶基因Glox。One of the objectives of the present invention is to provide a glucose oxidase gene Glox.
本发明的目的之二在于提供一种葡萄糖氧化酶基因Glox的制备方法。The second object of the present invention is to provide a method for preparing the glucose oxidase gene Glox.
本发明的目的之三在于提供一种利用葡萄糖氧化酶基因Glox编码的蛋白。The third object of the present invention is to provide a protein encoded by the glucose oxidase gene Glox.
本发明的目的之四在于提供一种利用葡萄糖氧化酶基因Glox转化的巴斯德毕赤酵母Pichia pastoris。The fourth object of the present invention is to provide a Pichia pastoris transformed with the glucose oxidase gene Glox.
本发明的目的之五在于提供一种利用葡萄糖氧化酶基因Glox转化毕赤酵母基因工程菌的方法。The fifth object of the present invention is to provide a method for transforming Pichia pastoris genetically engineered bacteria using the glucose oxidase gene Glox.
本发明的整体技术构思是:Overall technical idea of the present invention is:
葡萄糖氧化酶基因Glox,其基因序列为SEQ ID No.1。Glucose oxidase gene Glox, its gene sequence is SEQ ID No.1.
葡萄糖氧化酶基因Glox的制备方法,是以5′端ATGAAGCTCCTTGGCCTCC和3′端CTAATTAACAGTAGCGTTGTAATC为特异引物,以扩展青霉DNA为模板,采用PCR扩增方法获得。The preparation method of the glucose oxidase gene Glox is obtained by using the 5' end ATGAAGCTCCTTGGCCTCC and the 3' end CTAATTAACAGTAGCGTTGTAATC as specific primers, using the Penicillium sp. DNA as a template, and obtaining it by PCR amplification.
利用萄萄糖氧化酶基因Glox编码的蛋白,其序列为SEQ ID No.2。The sequence of the protein encoded by the glucose oxidase gene Glox is SEQ ID No.2.
利用葡萄糖氧化酶基因Glox转化的毕赤酵母基因工程菌,其保藏编号为CGMCCNo.13358。The Pichia pastoris genetically engineered strain transformed with the glucose oxidase gene Glox has a preservation number of CGMCC No. 13358.
本发明中的毕赤酵母基因工程菌申请人已于2016年11月30日提交中国微生物菌种保藏管理委员会普通微生物中心保藏,保藏编号为CGMCC No.13358,该保藏机构的地址位于北京市朝阳区北辰西路1号院3号中国科学院微生物研究所,该保藏机构的简称为CGMCC。The Pichia genetically engineered bacterium in the present invention has been submitted by the applicant to the General Microorganism Center of China Microbiological Culture Collection Management Committee on November 30, 2016. The deposit number is CGMCC No.13358. The address of the depository institution is located in Chaoyang, Beijing. Institute of Microbiology, Chinese Academy of Sciences, No. 1, Yard 1, Beichen West Road, District. The abbreviation of this depository institution is CGMCC.
利用葡萄糖氧化酶基因Glox转化的毕赤酵母基因工程菌的制备方法,其制备方法中的步骤如下:Utilize the preparation method of the Pichia pastoris genetic engineering bacterium transformed by glucose oxidase gene Glox, the steps in its preparation method are as follows:
a、通过PCR方法设计引物将将扩展青霉的葡萄糖氧化酶基因序列中的信号肽编码序列去除,引物序列如下:Glox-F:5′GGCTGAAGCTTACGTAGAATTC CTTCCACAAGCTGACTTCGACC3′;序列中下划线部分为上游引物添加限制性内切酶EcoRI识别位点;Glox-R:5′GAGATGAGTTTTTGTTCTAGAGCGGCCGCCTAATTAA CAGTAGCGTTGTAATC 3′;序列中下划线部分为下游添加限制性内切酶NotI识别位点;a. Design primers by PCR method to remove the signal peptide coding sequence in the glucose oxidase gene sequence of Penicillium elongatus. The primer sequence is as follows: Glox-F: 5'GGCTGAAGCTTACGTAGAATTCCTTCCACAAGCTGACTTCGACC3'; the underlined part in the sequence is the upstream primer to add restrictions Endonuclease EcoRI recognition site; Glox-R: 5'GAGATGAGTTTTTGTTCTAGAGCGGCCGCCTAATTAA CAGTAGCGTTGTAATC 3'; the underlined part in the sequence is the restriction endonuclease NotI recognition site added downstream;
b、PCR产物经纯化回收采GIBSON连接到表达载体pMD-AOX的EcoRI和NotI位点上,转化到E.coli DH5α,酶切验证筛选阳性克隆,并送测序;b. After purification and recovery, the PCR product was connected to the EcoRI and NotI sites of the expression vector pMD-AOX with GIBSON, transformed into E.coli DH5α, verified by restriction enzyme digestion, screened positive clones, and sent for sequencing;
c、测序正确重组质粒pMD-AOX-Glox经PmeI酶切后线性化,用2μg线性化pMD-AOX-Glox质粒电击转化80μl毕赤酵母Pichia pastoris X33感受态细胞,然后将转化细胞涂于含100μg/mlG418的YPDS平板上,30℃培养96h;获得巴斯德毕赤酵母Pichia pastorisCGMCC No.13358。c. The sequencing is correct. The recombinant plasmid pMD-AOX-Glox is linearized after digestion with PmeI, and 80 μl of Pichia pastoris X33 competent cells are transformed by electroporation with 2 μg of the linearized pMD-AOX-Glox plasmid, and then the transformed cells are spread on a medium containing 100 μg /mlG418 on a YPDS plate, cultured at 30°C for 96 hours; Pichia pastorisCGMCC No.13358 was obtained.
巴斯德毕赤酵母Pichia pastoris CGMCC No.13358在制备葡萄糖氧化酶中的应用。Application of Pichia pastoris CGMCC No.13358 in preparing glucose oxidase.
本发明的具体技术构思还有:Concrete technical concept of the present invention also has:
巴斯德毕赤酵母Pichia pastoris CGMCC No.13358在制备葡萄糖氧化酶中的应用,包括如下工艺步骤:The application of Pichia pastoris CGMCC No.13358 in the preparation of glucose oxidase comprises the following process steps:
A、将巴斯德毕赤酵母Pichia pastoris CGMCC No.13358接种于无菌的YPD培养基培养12-16h;A. Inoculate Pichia pastoris CGMCC No.13358 in sterile YPD medium for 12-16 hours;
B、按体积比为3%接种量将步骤A培养后的菌种转接于体积为100ml的无菌BMGY培养基,在温度为30℃的条件下摇瓶培养至OD600≈6-7;B. Transfer the bacteria cultured in step A to a sterile BMGY medium with a volume of 100ml according to the volume ratio of 3% inoculum, and shake the flask at a temperature of 30°C until OD 600 ≈6-7;
C、按照10%的体积比将步骤B中的培养后的菌种接种于盛有无菌BSM的培养基的发酵罐中,在温度为30℃、转速550转/分钟、pH=5的条件下培养至菌体OD600≈90;C. Inoculate the cultured strains in step B in a fermenter filled with sterile BSM medium at a volume ratio of 10%, under the conditions of 30°C, 550 rpm, and pH=5 Cultivate until the cell OD 600 ≈90;
D、流加50%甘油,每升甘油中含12mLPTM1,流加速度为12mL/h/L,温度为30℃的条件下培养4h,OD600≈150-170,停止补料0.5-1h,确认甘油耗尽;D. Feed 50% glycerol, each liter of glycerin contains 12mL PTM1, the flow rate is 12mL/h/L, and the temperature is 30°C, culture for 4h, OD 600 ≈150-170, stop feeding for 0.5-1h, confirm glycerol run out
E、按照流加速度为3.0mL-5.0mL/h/L流加入诱导剂甲醇,每升甲醇中含12mLPTM1,pH用氨水维持在6.0-6.5,每隔12小时取样测定酶活,当酶活出现下降的拐点时中止发酵。E. Add the inducer methanol according to the flow rate of 3.0mL-5.0mL/h/L. Each liter of methanol contains 12mL of PTM1, the pH is maintained at 6.0-6.5 with ammonia water, and the enzyme activity is measured every 12 hours. When the enzyme activity occurs Fermentation was stopped at the inflection point of decline.
本发明所取得的实质性特点和显著的技术进步在于:The substantive characteristics and remarkable technical progress that the present invention obtains are:
1、本发明通过PCR技术获得了一个全长的Glox基因序列,该基因全长为1815bp,GC含量为47.6%。同源分析该基因与以往的报道的GOD的基因序列同源性为94.71%,证明该基因是一个新的葡萄糖氧化酶基因。1. The present invention obtains a full-length Glox gene sequence through PCR technology, the full-length of the gene is 1815bp, and the GC content is 47.6%. Homology analysis showed that the sequence homology between this gene and the previously reported GOD gene was 94.71%, which proved that this gene was a new glucose oxidase gene.
2、传统青霉菌发酵生产GOD过程中,不仅存在夹杂大量过氧化氢酶、纤维素酶及淀粉酶等杂酶,难纯化的问题。利用本发明所获得的转基因毕赤酵母工程菌能够实现葡萄糖氧化酶的异源高效表达,并且毕赤酵母表达外源蛋白具有稳定性好、培养成本低和产物易分离纯化等优点。2. In the process of traditional Penicillium fermentation to produce GOD, there is not only a large amount of mixed enzymes such as catalase, cellulase and amylase, which are difficult to purify. The transgenic Pichia pastoris engineered bacteria obtained by the present invention can realize heterologous high-efficiency expression of glucose oxidase, and the expression of foreign protein by Pichia pastoris has the advantages of good stability, low culture cost, easy separation and purification of products, and the like.
3、经申请人试验证实,本发明所获得的转基因毕赤酵母工程菌在10L发酵罐发酵酶活达到305U/mL,并且条带单一,获得萄糖氧化酶准确高效的生产,大大降低了后处理的成本,为后期的工业化生产提供了导向基础,大大提高经济效益。3. It has been confirmed by the applicant's test that the fermented enzyme activity of the transgenic Pichia pastoris obtained in the present invention reaches 305U/mL in a 10L fermenter, and the band is single, and the accurate and efficient production of glucose oxidase is obtained, which greatly reduces the after-effects. The cost of processing provides a guiding basis for later industrial production and greatly improves economic benefits.
附图说明Description of drawings
本发明的附图有:Accompanying drawing of the present invention has:
图1是本发明中葡萄糖氧化酶基因Glox及利用其编码的蛋白的序列表。Fig. 1 is the sequence listing of the glucose oxidase gene Glox and the protein encoded by it in the present invention.
图2扩展青霉Glox基因全长结果。Figure 2 Expands the full-length results of the Penicillium Glox gene.
以扩展青霉基因组DNA为模板,设计特异引物进行PCR扩增,扩增出现一条小于2000bp的特异条带,序列分析表明该片段长1815bp。M为DNA Marker,分子量从大到小依次为10000bp,5000bp,3000bp,2000bp,1500bp,1000bp,750bp,500bp,250bp,100bp;1为Glox基因扩增产物。Using Genomic DNA of Penicillium elongatum as a template, specific primers were designed for PCR amplification, and a specific band less than 2000bp was amplified, and the sequence analysis showed that the fragment was 1815bp long. M is DNA Marker, the molecular weight from large to small is 10000bp, 5000bp, 3000bp, 2000bp, 1500bp, 1000bp, 750bp, 500bp, 250bp, 100bp; 1 is the Glox gene amplification product.
图3是表达质粒pMD-AOX-GLOX双酶切检测结果。Figure 3 is the result of double enzyme digestion detection of the expression plasmid pMD-AOX-GLOX.
将经引物Glox-F和Glox-R进行PCR扩增并纯化回收的扩展青霉Glox基因和经过EcoRI和NotI双酶切的载体pMD-AOX进行Gibson连接以构建重组质粒。用重组质粒转化感受态大肠杆菌DH5α,并在含Amp的LB平板上筛选阳性菌落。阳性菌落质粒经EcoRI和NotI双酶切后,得到约6.5.0kb和1.8kb的两个DNA片段,亦与预期大小相符。图中M为DNA Marker,分子量从大到小依次为10000bp,8000bp,6000bp,5000bp,4000bp,3000bp,2000bp,1000bp,1-6是表达质粒pMD-AOX-Glox双酶切产物。The Penicillium elongata Glox gene recovered by PCR amplification and purification with primers Glox-F and Glox-R and the vector pMD-AOX cut with EcoRI and NotI were subjected to Gibson ligation to construct a recombinant plasmid. Transform competent Escherichia coli DH5α with the recombinant plasmid, and screen positive colonies on LB plates containing Amp. After the positive colony plasmid was digested with EcoRI and NotI, two DNA fragments of about 6.5.0kb and 1.8kb were obtained, which were also in line with the expected size. In the figure, M is DNA Marker, the molecular weight from large to small is 10000bp, 8000bp, 6000bp, 5000bp, 4000bp, 3000bp, 2000bp, 1000bp, 1-6 is the product of double enzyme digestion of the expression plasmid pMD-AOX-Glox.
图4是葡萄糖氧化酶在YPCS的表达的SDS-PAGE检测结果。Fig. 4 is the SDS-PAGE detection result of the expression of glucose oxidase in YPCS.
将重组的表达质粒pMD-AOX-Glox经PmeI酶切后线性化后,电转化毕赤酵母X33感受态,在YPDS平板生长3d后,随机挑选阳性菌落转接液体YPCS,经甲醇诱导72h后,测定发酵液上清中的葡萄糖氧化酶活性,同时发酵液上清液做蛋白质SDS-PAGE电泳,可见一条浓染的约80kD的蛋白条带,几乎没有其余杂带。图中Marker为蛋白Marker,分子量从大到小依次是220kD,135kD,90kD,66kD,45kD,35kD,29kD,20kD,14kD,1-3是发酵上清液稀释10倍,4-6是发酵上清液稀释5倍。The recombinant expression plasmid pMD-AOX-Glox was digested with PmeI and linearized, then electrotransformed Pichia pastoris X33 competent, after growing on the YPDS plate for 3 days, randomly selected positive colonies were transferred to liquid YPCS, and induced by methanol for 72 hours, The glucose oxidase activity in the supernatant of the fermentation broth was measured, and at the same time, the supernatant of the fermentation broth was subjected to protein SDS-PAGE electrophoresis, and a densely stained protein band of about 80kD was seen, with almost no other miscellaneous bands. Marker in the figure is a protein marker, and its molecular weight from large to small is 220kD, 135kD, 90kD, 66kD, 45kD, 35kD, 29kD, 20kD, 14kD, 1-3 is the 10-fold dilution of the fermentation supernatant, 4-6 is the fermentation supernatant The supernatant was diluted 5 times.
图5是葡萄糖氧化酶在10L发酵罐的表达SDS-PAGE检测结果。Figure 5 is the SDS-PAGE detection result of the expression of glucose oxidase in a 10L fermenter.
在10L发酵罐中,在甲醇未诱导之前,处于菌株培养和碳源饲喂阶段,在这两个阶段内,菌体大量增长,此时无葡萄糖氧化酶蛋白的表达。随着甲醇的诱导,发酵液中的葡萄糖氧化酶活性逐渐增加,诱导144h后发酵液中葡萄糖氧化酶活性为305U/ml,蛋白质表达量达到5.2g,SDS-PAGE同时表明发酵液中葡萄糖氧化酶蛋白表达量也在不断积累。图中M为蛋白Marker,1-14为经甲醇诱导0h,24h,36h,48h,60h,72h,84h,96h,108h,120h,132h,144h,156h,168h葡萄糖氧化酶表达量。In the 10L fermenter, before methanol was not induced, it was in the stage of strain cultivation and carbon source feeding. In these two stages, the bacteria grew in large quantities, and there was no expression of glucose oxidase protein at this time. With the induction of methanol, the activity of glucose oxidase in the fermentation broth gradually increased. After 144 hours of induction, the activity of glucose oxidase in the fermentation broth was 305U/ml, and the protein expression reached 5.2g. SDS-PAGE also showed that the glucose oxidase in the fermentation broth Protein expression is also accumulating. In the figure, M is the protein marker, 1-14 is the expression level of glucose oxidase induced by methanol at 0h, 24h, 36h, 48h, 60h, 72h, 84h, 96h, 108h, 120h, 132h, 144h, 156h, and 168h.
具体实施方式Detailed ways
以下结合附图对本发明的实施例作进一步描述,但不作为对本发明的限定。本发明的保护范围以权利要求记载的内容为准,任何依据说明书作出的等效技术手段替换,均不脱离本发明的保护范畴。Embodiments of the present invention will be further described below in conjunction with the accompanying drawings, but they are not intended to limit the present invention. The scope of protection of the present invention is based on the contents of the claims, and any replacement of equivalent technical means based on the specification does not depart from the scope of protection of the present invention.
实施例1重组菌的构建及鉴定Construction and Identification of Embodiment 1 Recombinant Bacteria
选取实验室之前保存的扩展青霉Penicillium expansum CICC 40658,获得酶活稳定和较高的菌株,以此菌株的基因为模版设计引物,获得基因Glox。将纯化后的PCR产物采用Gibson方法与穿梭载体pMD-AOX连接,连接完成后转化大肠杆菌DH5α感受态细胞,挑取转化平板上的白色阳性克隆菌,获得含有Glox基因的重组表达质粒pMD-AOX-Glox。用双酶切进行验证。Select the Penicillium expansum CICC 40658 previously preserved in the laboratory to obtain a strain with stable and high enzyme activity, and use the gene of this strain as a template to design primers to obtain the gene Glox. The purified PCR product was connected with the shuttle vector pMD-AOX by the Gibson method. After the connection was completed, the E. coli DH5α competent cells were transformed, and the white positive clones on the transformation plate were picked to obtain the recombinant expression plasmid pMD-AOX containing the Glox gene. -Glox. Validation by double enzyme digestion.
将重组质粒pMD-AOX-Glox电击转化Pichia pastoris X33感受态细胞,得到基因工程菌Pichia pastoris X33-Glox。The recombinant plasmid pMD-AOX-Glox was electroporated to transform Pichia pastoris X33 competent cells to obtain genetically engineered bacteria Pichia pastoris X33-Glox.
毕赤酵母的转化采用电转化法:取X33划线培养过夜,在平板上挑取单菌落于5mLYPD中培养至OD600≈1.2,然后按照10%的接种量转接至50mL YPD摇瓶中,培养至OD600≈1.5;2500rpm离心5min,弃上清;将收集到的菌体用100mL 0.1M LiAc,100M DTT,0.6M山梨醇,10mM Tris-Hcl(pH=7.5)重悬,在30℃低速培养30min;再次2500rpm离心5min弃上清,用1M预冷的山梨醇反复洗3次,重悬于1.5mLBEDS中。80μL原生质体与5μL线性化质粒DNA(SacI切)混合,转入冰冷的电转杯,放置5分钟;电击细胞与DNA的混合物(1.5kv,3.0-4.9ms);将转化好的重组菌加入1M山梨醇,30℃静置2-5h;随后5000rpm离心2min,用生理盐水反复洗3次,涂布于固体YPDS(含G418)培养基。30℃培养72h挑取单菌落,获得巴斯德毕赤酵母Pichia pastoris CGMCC No.13358。The transformation of Pichia pastoris adopts the electroporation method: take X33 and culture overnight, pick a single colony on the plate and culture it in 5mLYPD to OD 600 ≈1.2, and then transfer it to a 50mL YPD shake flask according to the inoculum size of 10%. Cultivate until OD 600 ≈1.5; centrifuge at 2500rpm for 5min, discard the supernatant; resuspend the collected cells with 100mL 0.1M LiAc, 100M DTT, 0.6M sorbitol, 10mM Tris-Hcl (pH=7.5), at 30℃ Incubate at a low speed for 30 minutes; centrifuge again at 2500 rpm for 5 minutes to discard the supernatant, wash with 1M pre-cooled sorbitol repeatedly for 3 times, and resuspend in 1.5mL BEDS. Mix 80 μL protoplasts with 5 μL linearized plasmid DNA (cut with SacI), transfer to an ice-cold electroporation cuvette, and let stand for 5 minutes; electric shock the mixture of cells and DNA (1.5kv, 3.0-4.9ms); add the transformed recombinant bacteria to 1M Sorbitol, stand at 30°C for 2-5h; then centrifuge at 5000rpm for 2min, wash with saline repeatedly for 3 times, and spread on solid YPDS (containing G418) medium. After culturing at 30°C for 72 hours, a single colony was picked to obtain Pichia pastoris CGMCC No.13358.
实施例2重组菌的酶活测定和蛋白电泳Enzyme activity assay and protein electrophoresis of embodiment 2 recombinant bacteria
以实施例1获得的巴斯德毕赤酵母Pichia pastoris CGMCC No.13358为生产菌,活化后在30℃、200rpm条件下培养至OD600≈1.2的种子培养液以2%的接种量转入YPCS培养基,于30℃、200rpm条件下培养;在YPCS培养基中培养至OD600≈1.2时,将酵母细胞转入YPCS诱导培养基,每天添加1%甲醇连续诱导表达72h。Using the Pichia pastoris CGMCC No.13358 obtained in Example 1 as the production bacteria, after activation, the seed culture solution cultivated to OD 600 ≈ 1.2 under the conditions of 30°C and 200rpm was transferred to YPCS with an inoculum of 2%. Culture medium, cultivated at 30°C and 200rpm; when cultured in YPCS medium to OD 600 ≈1.2, yeast cells were transferred to YPCS induction medium, and 1% methanol was added every day to continuously induce expression for 72 hours.
培养基culture medium
种子和斜面培养基为YPD培养基:胰蛋白胨2%,酵母提取物1%,葡萄糖2%;斜面培养基添加琼脂2%。The seed and slant medium are YPD medium: 2% tryptone, 1% yeast extract, 2% glucose; 2% agar is added to the slant medium.
YPCS培养基:胰蛋白胨2%,酵母提取物1%,酪蛋白水解物2%,山梨醇0.5%。YPCS medium: tryptone 2%, yeast extract 1%, casein hydrolyzate 2%, sorbitol 0.5%.
通过蛋白电泳(SDS-PAGE)得到一条如图4所示分子量大小约为80kDa的蛋白条带。A protein band with a molecular weight of about 80 kDa was obtained by protein electrophoresis (SDS-PAGE) as shown in FIG. 4 .
葡萄糖氧化酶酶活测定方法:葡萄糖氧化酶活性测定一般采用邻一联(二)茴香胺分光光度法。在3mL的反应体系中,包含0.5mol/L醋酸缓冲液(pH=5.1),0.17mmol/L邻联茴香胺溶液和1.72%葡萄糖溶液及0.1mg/mL辣根过氧化物酶,35℃震荡混匀,加入0.1mL葡萄糖氧化酶溶液,用分光光度计,于A=500nm自动记录随时间变化的吸光度值,根据公式X=(ΔA500×3.1×df)/(7.5×0.1),计算葡萄糖氧化酶活力单位。Glucose oxidase enzyme activity assay method: The glucose oxidase activity assay generally adopts the o-one (two) anisidine spectrophotometric method. In a 3mL reaction system containing 0.5mol/L acetate buffer (pH=5.1), 0.17mmol/L o-dianisidine solution, 1.72% glucose solution and 0.1mg/mL horseradish peroxidase, shake at 35°C Mix well, add 0.1mL glucose oxidase solution, and use a spectrophotometer to automatically record the absorbance value changing with time at A=500nm, and calculate the glucose oxidation according to the formula X=(ΔA500×3.1×df)/(7.5×0.1). Enzyme activity unit.
X:样品酶活(U/mL);X: sample enzyme activity (U/mL);
ΔA500为活度值;ΔA500 is the activity value;
3.1:反应体积;3.1: Reaction volume;
df为稀释倍数;df is the dilution factor;
7.5:葡萄糖内酯A500消光系数;7.5: Glucolactone A500 extinction coefficient;
0.1:加入酶液体积。0.1: Add the volume of enzyme solution.
实施例3重组菌株在10L发酵罐上酶活的验证The verification of embodiment 3 recombinant bacterial strains enzyme activity on 10L fermenter
A、将巴斯德毕赤酵母Pichia pastoris CGMCC No.13358接种于无菌的YPD培养基培养12-16h;A. Inoculate Pichia pastoris CGMCC No.13358 in sterile YPD medium for 12-16 hours;
B、按体积比为3%接种量将步骤A培养后的菌种转接于体积为100mL的无菌BMGY培养基,在温度为30℃的条件下摇瓶培养至OD600≈6-7;B. Transfer the bacteria cultured in step A to a sterile BMGY medium with a volume of 100mL at a volume ratio of 3% inoculum, and shake the flask at a temperature of 30°C until OD 600 ≈6-7;
C、按照10%的体积比将步骤B中的培养后的菌种接种于盛有无菌BSM的培养基的发酵罐中,在温度为30℃、转速550转/分钟、pH=5的条件下培养至菌体OD600≈90;C. Inoculate the cultured strains in step B in a fermenter filled with sterile BSM medium at a volume ratio of 10%, under the conditions of 30°C, 550 rpm, and pH=5 Cultivate until the cell OD 600 ≈90;
D、流加50%甘油,每升甘油中含12mLPTM1,流加速度为12mL/h/L,温度为30℃的条件下培养4h,OD600≈150-170,停止补料0.5-1h,确认甘油耗尽;D. Feed 50% glycerol, 12mL PTM1 per liter of glycerin, flow rate of 12mL/h/L, culture at 30°C for 4h, OD 600 ≈150-170, stop feeding for 0.5-1h, confirm glycerol run out
E、按照流加速度为3.0mL-5.0mL/h/L流加入诱导剂甲醇,每升甲醇中含PTM112mL,pH用氨水维持在6.0-6.5,每隔12小时取样测定酶活,当酶活出现下降的拐点时中止发酵。重组菌在10L发酵罐上的酶活最高可达到305U/mL。E. Add the inducer methanol according to the flow rate of 3.0mL-5.0mL/h/L, each liter of methanol contains PTM112mL, the pH is maintained at 6.0-6.5 with ammonia water, and the enzyme activity is measured every 12 hours. When the enzyme activity occurs Fermentation was stopped at the inflection point of decline. The highest enzyme activity of recombinant bacteria in 10L fermenter can reach 305U/mL.
培养基和试剂Media and Reagents
BMGY培养基:酵母提取物1%;蛋白胨2%;磷酸钾pH6.0 100mM;YNB1.34%;生物素4×10-5%;甘油1%或甲醇0.5%。BMGY medium: yeast extract 1%; peptone 2%; potassium phosphate pH6.0 100mM; YNB1.34%; biotin 4×10-5%; glycerol 1% or methanol 0.5%.
PTM1(微量元素):硫酸铜6.0g/L;碘化钠0.08g/L;硫酸锰3.0g/L;钼酸钠0.2g/L;硼酸0.02g/L;氯化钴0.5g/L;氯化锌20g/L;硫酸亚铁65g/L;硫酸5.0mL/L;生物素0.2g/L;VC80mg/L;VB20.5M。PTM1 (trace elements): copper sulfate 6.0g/L; sodium iodide 0.08g/L; manganese sulfate 3.0g/L; sodium molybdate 0.2g/L; boric acid 0.02g/L; cobalt chloride 0.5g/L; Zinc chloride 20g/L; ferrous sulfate 65g/L; sulfuric acid 5.0mL/L; biotin 0.2g/L; V C 80mg/L; V B2 0.5M.
BSM培养基:85%H3PO4 26.7mL/L;CaSO4 0.93g/L;K2SO4 18.2g/L;MgSO4·7H2O14.9g/L;KOH 4.13g/L;甘油40g/L;PTM14.35mL/L(过滤除菌)。BSM medium: 85% H 3 PO 4 26.7mL/L; CaSO 4 0.93g/L; K 2 SO 4 18.2g/L; MgSO 4 ·7H 2 O 14.9g/L; KOH 4.13g/L; Glycerol 40g /L; PTM14.35mL/L (sterilized by filtration).
序列表 sequence listing
<110> 河北省微生物研究所<110> Hebei Institute of Microbiology
中国科学院微生物研究所 Institute of Microbiology, Chinese Academy of Sciences
<120> 葡萄糖氧化酶基因Glox、蛋白、巴斯德毕赤酵母及其制备和应用<120> Glucose oxidase gene Glox, protein, Pichia pastoris and its preparation and application
<130> 201510893562.8;CN105936910A;CN106591249A;CN105950577A<130> 201510893562.8; CN105936910A; CN106591249A; CN105950577A
<160> 2<160> 2
<170> SIPOSequenceListing 1.0<170> SIPOSequenceListing 1.0
<210> 1<210> 1
<211> 1815<211> 1815
<212> DNA<212>DNA
<213> An artificial sequence<213> An artificial sequence
<400> 1<400> 1
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tccttctcac caatgattaa atctttgatg aagaacgcta ataactctgg tattcctgtc 660tccttctcac caatgattaa atctttgatg aagaacgcta ataactctgg tattcctgtc 660
caaaaagatt tgggatgtgg agttcctcac ggaatttcaa tgattttgaa tgacgtccac 720caaaaagatt tgggatgtgg agttcctcac ggaatttcaa tgattttgaa tgacgtccac 720
gaggatcaaa ctagatccga tgctgctcgt gagtggcttc tgcctaacta ccagagatcc 780gaggatcaaa ctagatccga tgctgctcgt gagtggcttc tgcctaacta ccagagatcc 780
aatcttaaga tcctgactgg acaaatggtt ggtaaggtgc tgtttgatac caccactact 840aatcttaaga tcctgactgg acaaatggtt ggtaaggtgc tgtttgatac caccactact 840
actccaaaag ccgtcggtgt gaattttggt actcacgcca aggtcaactt cgacgtgcac 900actccaaaag ccgtcggtgt gaattttggt actcacgcca aggtcaactt cgacgtgcac 900
gctagacacg aagttttgct tgcttctggt tccgccgttt ctccacagat tctggagcat 960gctagacacg aagttttgct tgcttctggt tccgccgttt ctccacagat tctggagcat 960
tccggagttg gtcttaaggc tgtcctggat aacgtcggtg ttgaacagtt ggttgatctt 1020tccggagttg gtcttaaggc tgtcctggat aacgtcggtg ttgaacagtt ggttgatctt 1020
ccagtcggtt tgaacctgca ggaccaaact actactaccg ttagatccaa cattaattct 1080ccagtcggtt tgaacctgca ggaccaaact actactaccg ttagatccaa cattaattct 1080
attggtgctg gacagggtca agctgcttac tttgccactt tcaacgaaac ctttggtgat 1140attggtgctg gacagggtca agctgcttac tttgccactt tcaacgaaac ctttggtgat 1140
caagctccac gtgctcatca gttgttgaac actaagctgg aggagtgggc taaggacgtt 1200caagctccac gtgctcatca gttgttgaac actaagctgg aggagtgggc taaggacgtt 1200
gtttctagag gtggtttcca caacgaaacc gctcttcttg tccagtacga gaactacaga 1260gtttctagag gtggtttcca caacgaaacc gctcttcttg tccagtacga gaactacaga 1260
gactggttgg ttaacgagga cgtctccttt gctgagattt tcatcgatac cgccggaaag 1320gactggttgg ttaacgagga cgtctccttt gctgagattt tcatcgatac cgccggaaag 1320
ttgaatctgg acctgtggga tcttattcca tttactcgtg gatatgttca catcctggat 1380ttgaatctgg acctgtggga tcttattcca tttactcgtg gatatgttca catcctggat 1380
tcagatccat atttgagaag attcgcctat gacccacagt tcttcctgaa cgagcttgac 1440tcagatccat atttgagaag attcgcctat gacccacagt tcttcctgaa cgagcttgac 1440
gttcttggtc aagccgctgc ctccaaactg gccagagaga tttccaacac cggtgaaatg 1500gttcttggtc aagccgctgc ctccaaactg gccagagaga tttccaacac cggtgaaatg 1500
acccaatatt tcaatggtga agccatccca ggtaataacc ttgcctacaa cgccactctt 1560acccaatatt tcaatggtga agccatccca ggtaataacc ttgcctacaa cgccactctt 1560
gacgactggg ttgatcacgt taagcagaac tttcgtgcta actaccatgg tgtcggaacc 1620gacgactggg ttgatcacgt taagcagaac tttcgtgcta actaccatgg tgtcggaacc 1620
tgttccatga tgtctaagga gttgggtggt gttgttgacg ccgctgctcg tgtgtacggt 1680tgttccatga tgtctaagga gttgggtggt gttgttgacg ccgctgctcg tgtgtacggt 1680
gttgagtccc ttagagtcat cgatggttcc attcctccaa cccaactttc ttcccatgtt 1740gttgagtccc ttagagtcat cgatggttcc attcctccaa cccaactttc ttcccatgtt 1740
atgaccgtgt tttacggaat ggcccaaaaa gtttcagagg ccattttggc cgattacaac 1800atgaccgtgt tttacggaat ggcccaaaaa gtttcagagg ccattttggc cgattacaac 1800
gctactgtta attag 1815gctactgtta attag 1815
<210> 2<210> 2
<211> 588<211> 588
<212> PRT<212> PRT
<213> An artificial sequence<213> An artificial sequence
<400> 2<400> 2
Leu Pro Gln Ala Asp Phe Asp Leu Gln Ser Ser Leu Leu Thr Asp ProLeu Pro Gln Ala Asp Phe Asp Leu Gln Ser Ser Leu Leu Thr Asp Pro
1 5 10 151 5 10 15
Thr Lys Val Ala Gly Thr Thr Phe Asp Tyr Ile Ile Ala Gly Gly GlyThr Lys Val Ala Gly Thr Thr Phe Asp Tyr Ile Ile Ala Gly Gly Gly
20 25 30 20 25 30
Leu Thr Gly Leu Thr Val Ala Ala Arg Leu Thr Glu Asn Pro Asn IleLeu Thr Gly Leu Thr Val Ala Ala Arg Leu Thr Glu Asn Pro Asn Ile
35 40 45 35 40 45
Thr Val Leu Val Ile Glu Arg Gly Phe Tyr Glu Ser Asn Ile Gly ProThr Val Leu Val Ile Glu Arg Gly Phe Tyr Glu Ser Asn Ile Gly Pro
50 55 60 50 55 60
Ile Ile Glu Asn Leu Asn His Tyr Gly Asp Ile Phe Gly Thr Ser ValIle Ile Glu Asn Leu Asn His Tyr Gly Asp Ile Phe Gly Thr Ser Val
65 70 75 8065 70 75 80
Asp Gln Ala Phe Glu Thr Ile Pro Leu Ala Ile His Asn Arg Thr GluAsp Gln Ala Phe Glu Thr Ile Pro Leu Ala Ile His Asn Arg Thr Glu
85 90 95 85 90 95
Ile Val Arg Ser Gly Lys Gly Leu Gly Gly Ser Thr Leu Val Asn GlyIle Val Arg Ser Gly Lys Gly Leu Gly Gly Ser Thr Leu Val Asn Gly
100 105 110 100 105 110
Gly Ser Trp Thr Arg Pro His Lys Ala Gln Val Asp Ser Trp Glu SerGly Ser Trp Thr Arg Pro His Lys Ala Gln Val Asp Ser Trp Glu Ser
115 120 125 115 120 125
Val Phe Gly Met Glu Gly Trp Asn Trp Asp Ser Leu Leu Pro Tyr MetVal Phe Gly Met Glu Gly Trp Asn Trp Asp Ser Leu Leu Pro Tyr Met
130 135 140 130 135 140
Lys Lys Ile Glu Ala Ala Arg Ala Pro Asn Ala Glu Gln Ile Ala AlaLys Lys Ile Glu Ala Ala Arg Ala Pro Asn Ala Glu Gln Ile Ala Ala
145 150 155 160145 150 155 160
Gly His Tyr Tyr Asp Pro Ser Cys His Gly Thr Asp Gly Ile Val HisGly His Tyr Tyr Asp Pro Ser Cys His Gly Thr Asp Gly Ile Val His
165 170 175 165 170 175
Val Gly Pro Arg Asp Thr Gly Glu Ser Phe Ser Pro Met Ile Lys SerVal Gly Pro Arg Asp Thr Gly Glu Ser Phe Ser Pro Met Ile Lys Ser
180 185 190 180 185 190
Leu Met Lys Asn Ala Asn Asn Ser Gly Ile Pro Val Gln Lys Asp LeuLeu Met Lys Asn Ala Asn Asn Ser Gly Ile Pro Val Gln Lys Asp Leu
195 200 205 195 200 205
Gly Cys Gly Val Pro His Gly Ile Ser Met Ile Leu Asn Asp Val HisGly Cys Gly Val Pro His Gly Ile Ser Met Ile Leu Asn Asp Val His
210 215 220 210 215 220
Glu Asp Gln Thr Arg Ser Asp Ala Ala Arg Glu Trp Leu Leu Pro AsnGlu Asp Gln Thr Arg Ser Asp Ala Ala Arg Glu Trp Leu Leu Pro Asn
225 230 235 240225 230 235 240
Tyr Gln Arg Ser Asn Leu Lys Ile Leu Thr Gly Gln Met Val Gly LysTyr Gln Arg Ser Asn Leu Lys Ile Leu Thr Gly Gln Met Val Gly Lys
245 250 255 245 250 255
Val Leu Phe Asp Thr Thr Thr Thr Thr Pro Lys Ala Val Gly Val AsnVal Leu Phe Asp Thr Thr Thr Thr Thr Thr Pro Lys Ala Val Gly Val Asn
260 265 270 260 265 270
Phe Gly Thr His Ala Lys Val Asn Phe Asp Val His Ala Arg His GluPhe Gly Thr His Ala Lys Val Asn Phe Asp Val His Ala Arg His Glu
275 280 285 275 280 285
Val Leu Leu Ala Ser Gly Ser Ala Val Ser Pro Gln Ile Leu Glu HisVal Leu Leu Ala Ser Gly Ser Ala Val Ser Pro Gln Ile Leu Glu His
290 295 300 290 295 300
Ser Gly Val Gly Leu Lys Ala Val Leu Asp Asn Val Gly Val Glu GlnSer Gly Val Gly Leu Lys Ala Val Leu Asp Asn Val Gly Val Glu Gln
305 310 315 320305 310 315 320
Leu Val Asp Leu Pro Val Gly Leu Asn Leu Gln Asp Gln Thr Thr ThrLeu Val Asp Leu Pro Val Gly Leu Asn Leu Gln Asp Gln Thr Thr Thr
325 330 335 325 330 335
Thr Val Arg Ser Asn Ile Asn Ser Ile Gly Ala Gly Gln Gly Gln AlaThr Val Arg Ser Asn Ile Asn Ser Ile Gly Ala Gly Gln Gly Gln Ala
340 345 350 340 345 350
Ala Tyr Phe Ala Thr Phe Asn Glu Thr Phe Gly Asp Gln Ala Pro ArgAla Tyr Phe Ala Thr Phe Asn Glu Thr Phe Gly Asp Gln Ala Pro Arg
355 360 365 355 360 365
Ala His Gln Leu Leu Asn Thr Lys Leu Glu Glu Trp Ala Lys Asp ValAla His Gln Leu Leu Asn Thr Lys Leu Glu Glu Trp Ala Lys Asp Val
370 375 380 370 375 380
Val Ser Arg Gly Gly Phe His Asn Glu Thr Ala Leu Leu Val Gln TyrVal Ser Arg Gly Gly Phe His Asn Glu Thr Ala Leu Leu Val Gln Tyr
385 390 395 400385 390 395 400
Glu Asn Tyr Arg Asp Trp Leu Val Asn Glu Asp Val Ser Phe Ala GluGlu Asn Tyr Arg Asp Trp Leu Val Asn Glu Asp Val Ser Phe Ala Glu
405 410 415 405 410 415
Ile Phe Ile Asp Thr Ala Gly Lys Leu Asn Leu Asp Leu Trp Asp LeuIle Phe Ile Asp Thr Ala Gly Lys Leu Asn Leu Asp Leu Trp Asp Leu
420 425 430 420 425 430
Ile Pro Phe Thr Arg Gly Tyr Val His Ile Leu Asp Ser Asp Pro TyrIle Pro Phe Thr Arg Gly Tyr Val His Ile Leu Asp Ser Asp Pro Tyr
435 440 445 435 440 445
Leu Arg Arg Phe Ala Tyr Asp Pro Gln Phe Phe Leu Asn Glu Leu AspLeu Arg Arg Phe Ala Tyr Asp Pro Gln Phe Phe Leu Asn Glu Leu Asp
450 455 460 450 455 460
Val Leu Gly Gln Ala Ala Ala Ser Lys Leu Ala Arg Glu Ile Ser AsnVal Leu Gly Gln Ala Ala Ala Ser Lys Leu Ala Arg Glu Ile Ser Asn
465 470 475 480465 470 475 480
Thr Gly Glu Met Thr Gln Tyr Phe Asn Gly Glu Ala Ile Pro Gly AsnThr Gly Glu Met Thr Gln Tyr Phe Asn Gly Glu Ala Ile Pro Gly Asn
485 490 495 485 490 495
Asn Leu Ala Tyr Asn Ala Thr Leu Asp Asp Trp Val Asp His Val LysAsn Leu Ala Tyr Asn Ala Thr Leu Asp Asp Trp Val Asp His Val Lys
500 505 510 500 505 510
Gln Asn Phe Arg Ala Asn Tyr His Gly Val Gly Thr Cys Ser Met MetGln Asn Phe Arg Ala Asn Tyr His Gly Val Gly Thr Cys Ser Met Met
515 520 525 515 520 525
Ser Lys Glu Leu Gly Gly Val Val Asp Ala Ala Ala Arg Val Tyr GlySer Lys Glu Leu Gly Gly Val Val Asp Ala Ala Ala Arg Val Tyr Gly
530 535 540 530 535 540
Val Glu Ser Leu Arg Val Ile Asp Gly Ser Ile Pro Pro Thr Gln LeuVal Glu Ser Leu Arg Val Ile Asp Gly Ser Ile Pro Pro Thr Gln Leu
545 550 555 560545 550 555 560
Ser Ser His Val Met Thr Val Phe Tyr Gly Met Ala Gln Lys Val SerSer Ser His Val Met Thr Val Phe Tyr Gly Met Ala Gln Lys Val Ser
565 570 575 565 570 575
Glu Ala Ile Leu Ala Asp Tyr Asn Ala Thr Val AsnGlu Ala Ile Leu Ala Asp Tyr Asn Ala Thr Val Asn
580 585 580 585
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| CN110894219A (en) * | 2019-12-26 | 2020-03-20 | 河北省微生物研究所 | Pichia pastoris transcription factor HAC1, protein, pichia pastoris and preparation and application thereof |
| CN111334538A (en) * | 2020-03-20 | 2020-06-26 | 鄂州职业大学 | Method for producing gluconic acid by strengthening penicillium funiculosum fermentation glucose |
| CN111718862A (en) * | 2019-03-20 | 2020-09-29 | 中国科学院天津工业生物技术研究所 | High-throughput screening method of Pichia pastoris based on droplet microfluidic chip |
| CN112961791A (en) * | 2021-02-24 | 2021-06-15 | 华南理工大学 | Recombinant strain of non-specific peroxygenase and construction method and application thereof |
| CN115651918A (en) * | 2022-11-09 | 2023-01-31 | 河北省微生物研究所有限公司 | Method for improving yield of glucose oxidase |
| WO2023225459A2 (en) | 2022-05-14 | 2023-11-23 | Novozymes A/S | Compositions and methods for preventing, treating, supressing and/or eliminating phytopathogenic infestations and infections |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111718862A (en) * | 2019-03-20 | 2020-09-29 | 中国科学院天津工业生物技术研究所 | High-throughput screening method of Pichia pastoris based on droplet microfluidic chip |
| CN111718862B (en) * | 2019-03-20 | 2022-06-14 | 中国科学院天津工业生物技术研究所 | High-throughput pichia pastoris screening method based on droplet microfluidic chip |
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| CN111334538A (en) * | 2020-03-20 | 2020-06-26 | 鄂州职业大学 | Method for producing gluconic acid by strengthening penicillium funiculosum fermentation glucose |
| CN111334538B (en) * | 2020-03-20 | 2023-04-11 | 鄂州职业大学 | Method for producing gluconic acid by strengthening penicillium funiculosum fermentation glucose |
| CN112961791A (en) * | 2021-02-24 | 2021-06-15 | 华南理工大学 | Recombinant strain of non-specific peroxygenase and construction method and application thereof |
| WO2023225459A2 (en) | 2022-05-14 | 2023-11-23 | Novozymes A/S | Compositions and methods for preventing, treating, supressing and/or eliminating phytopathogenic infestations and infections |
| CN115651918A (en) * | 2022-11-09 | 2023-01-31 | 河北省微生物研究所有限公司 | Method for improving yield of glucose oxidase |
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