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CN110656055A - A kind of eukaryotic engineering strain and its preparation method and application - Google Patents

A kind of eukaryotic engineering strain and its preparation method and application Download PDF

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CN110656055A
CN110656055A CN201910911559.2A CN201910911559A CN110656055A CN 110656055 A CN110656055 A CN 110656055A CN 201910911559 A CN201910911559 A CN 201910911559A CN 110656055 A CN110656055 A CN 110656055A
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万霞
陈文超
黄凤洪
邓乾春
朱航志
蒋珊
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Abstract

本发明公开了一种真核工程菌株及其制备方法和应用,属于生物技术领域。所述真核工程菌株表达的蛋白为甘油二酯乙酰化转移酶,所述甘油二酯乙酰化转移酶的氨基酸序列表中SEQ ID NO:1所示。本发明提供了一种真核工程菌株及其制备方法和应用,该真核工程菌株能够大量合成乙酰化甘油三酯,可以通该真核工程菌株实现乙酰化甘油三酯的大规模生产,本发明实施例提供的制备方法能够获得大量的真核工程菌株,为乙酰化甘油三酯进行大规模生产提供基础,该应用包括将该真核工程菌株用于合成乙酰化甘油三酯。

Figure 201910911559

The invention discloses a eukaryotic engineering strain and a preparation method and application thereof, belonging to the field of biotechnology. The protein expressed by the eukaryotic engineering strain is diacylglycerol acetyltransferase, which is shown in SEQ ID NO: 1 in the amino acid sequence table of the diacylglycerol acetyltransferase. The invention provides a eukaryotic engineering strain and a preparation method and application thereof. The eukaryotic engineering strain can synthesize acetylated triglycerides in large quantities, and the eukaryotic engineering strain can realize large-scale production of acetylated triglycerides. The preparation method provided in the embodiment of the invention can obtain a large number of eukaryotic engineering strains, which provides a basis for large-scale production of acetylated triglycerides. The application includes using the eukaryotic engineering strains to synthesize acetylated triglycerides.

Figure 201910911559

Description

一种真核工程菌株及其制备方法和应用A kind of eukaryotic engineering strain and its preparation method and application

技术领域technical field

本发明涉及生物技术领域,特别涉及一种真核工程菌株及其制备方法和应用。The invention relates to the field of biotechnology, in particular to a eukaryotic engineering strain and a preparation method and application thereof.

背景技术Background technique

乙酰化甘油三酯是一种在sn-3端包含乙酰基团的特殊的甘油三酯。相较于常规的长链甘油三酯,乙酰化甘油三酯具有粘度低、在低温环境下活性好的优点,因此乙酰化甘油三酯能够直接应用于柴油当中作为生物燃料。另外,源于sn-3端的酰基,乙酰化甘油三酯能够作为1,2-二乙酸甘油三酯的半合成产物,这一类脂类能够应用于食物的乳化剂,润滑油,PVC的增塑剂和其他塑料制品。Acetylated triglycerides are specialized triglycerides that contain an acetyl group at the sn-3 terminus. Compared with conventional long-chain triglycerides, acetylated triglycerides have the advantages of low viscosity and good activity at low temperature, so acetylated triglycerides can be directly used in diesel fuel as biofuels. In addition, the acetylated triglyceride derived from the acyl group at the sn-3 end can be used as a semi-synthetic product of 1,2-diacetic acid triglyceride, which can be used in food emulsifiers, lubricating oils, and PVC additives. Plasticizers and other plastic products.

美国的Tam等人尝试用卫矛属(Euonymus)植物来源的乙酰化甘油三酯合成酶基因对亚麻荠(Camelina sativa)、大豆、拟南芥(Arabidopsis thaliana)和酿酒酵母(Saccharomyces cerevisiae)进行基因工程改造,得到重组酿酒酵母,利用该工程株合成乙酰化甘油三酯。Tam et al. in the United States tried to use the acetylated triglyceride synthase gene derived from Euonymus plants to transgenic Camelina sativa, soybean, Arabidopsis thaliana and Saccharomyces cerevisiae Through engineering transformation, a recombinant Saccharomyces cerevisiae is obtained, and the engineering strain is used to synthesize acetylated triglyceride.

在实现本发明的过程中,发明人发现现有技术至少存在以下问题:In the process of realizing the present invention, the inventor found that the prior art has at least the following problems:

重组酿酒酵母除了合成乙酰化甘油三酯外,同时还会合成常规的甘油三酯,每克样品中的乙酰化甘油三酯的量为2.4mg,且合成的乙酰化甘油三酯仅为每克重组酿酒酵母干重的0.24%左右,可见重组酿酒酵母合成的乙酰化甘油三酯产量较低,这不利于乙酰化甘油三酯的大规模生产。In addition to synthesizing acetylated triglycerides, the recombinant Saccharomyces cerevisiae also synthesized conventional triglycerides. The amount of acetylated triglycerides in each gram of the sample was 2.4 mg, and the synthesized acetylated triglycerides were only 2.4 mg per gram. About 0.24% of the dry weight of recombinant Saccharomyces cerevisiae, it can be seen that the yield of acetylated triglycerides synthesized by recombinant Saccharomyces cerevisiae is low, which is not conducive to the large-scale production of acetylated triglycerides.

发明内容SUMMARY OF THE INVENTION

为了解决现有技术的问题,本发明实施例提供了一种真核工程菌株及其制备方法和应用。所述技术方案如下:In order to solve the problems of the prior art, the embodiments of the present invention provide a eukaryotic engineering strain and a preparation method and application thereof. The technical solution is as follows:

一方面,本发明实施例提供了一种真核工程菌株,所述真核工程菌株表达的蛋白为甘油二酯乙酰化转移酶,所述甘油二酯乙酰化转移酶的氨基酸序列表中SEQ ID NO:1所示。On the one hand, the embodiment of the present invention provides a kind of eukaryotic engineering strain, the protein expressed by the eukaryotic engineering strain is diacylglycerol acetyltransferase, and SEQ ID in the amino acid sequence table of the diacylglycerol acetyltransferase NO:1 shown.

另一方面,本发明实施例提供了一种如上所述的真核工程菌株的制备方法,所述制备方法包括:On the other hand, the embodiment of the present invention provides a preparation method of the above-mentioned eukaryotic engineering strain, and the preparation method comprises:

将经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT与载体连接,得到连接产物;connecting the codon-optimized diglyceride acetyltransferase encoding gene EfDAcT with the carrier to obtain a ligated product;

将所述连接产物转入感受态细胞中,得到第一转化产物;transferring the ligation product into competent cells to obtain the first transformation product;

将所述第一转化产物于37℃下摇床培养0.6~1h,得到第一复苏液;The first transformation product is incubated at 37°C in a shaker for 0.6 to 1 hour to obtain a first resuscitation solution;

将所述第一复苏液涂布在含氨苄青霉素抗性的固体培养基上,于37℃下培养8~12h,得到转化子;Coating the first resuscitation solution on a solid medium containing ampicillin resistance, and culturing at 37°C for 8-12 hours to obtain transformants;

提取所述转化子的质粒,将所述质粒进行酶切,得到酶切产物;The plasmid of the transformant is extracted, and the plasmid is digested to obtain the digested product;

将所述酶切产物转入解脂耶氏酵母感受态细胞中,得到第二转化产物;Transferring the enzyme cleavage product into Yarrowia lipolytica competent cells to obtain a second transformation product;

将所述第二转化产物在酵母浸出粉胨葡萄糖液体培养基中于28℃下摇床培养0.6~1.2h,得到第二复苏液;The second transformation product is cultured in a yeast extract peptone glucose liquid medium at 28° C. in a shaker for 0.6-1.2 hours to obtain a second resuscitation solution;

将所述第二复苏液涂布在酵母菌完全补充混合培养基上,于37℃下培养8~12h,得到所述真核工程菌株。The second resuscitation solution is coated on the yeast complete supplemented mixed medium, and cultured at 37° C. for 8-12 hours to obtain the eukaryotic engineering strain.

具体地,所述EfDAcT基因的制备方法包括:将合成的EfDAcT基因序列作为cDNA模板,利用上游引物和下游引物进行扩增,得到所述EfDAcT基因,所述上游引物的序列如序列表中SEQ ID NO:2所示,所述下游引物的序列如序列表中SEQ ID NO:3所示。Specifically, the preparation method of the EfDAcT gene comprises: using the synthesized EfDAcT gene sequence as a cDNA template, using an upstream primer and a downstream primer to amplify to obtain the EfDAcT gene, and the sequence of the upstream primer is as SEQ ID in the sequence table. As shown in NO: 2, the sequence of the downstream primer is shown in SEQ ID NO: 3 in the sequence listing.

具体地,采用热击法将所述连接产物转入所述感受态细胞中。Specifically, the ligation product is transferred into the competent cells by heat shock method.

进一步地,所述热击法包括:将所述连接产物和所述感受态细胞混合后,置于冰上30~40min,得到混合液,将所述混合液置于42℃水浴锅中热击45s后,在冰上冷却2min,得到所述转化产物。Further, the heat shock method includes: after mixing the ligation product and the competent cells, placing it on ice for 30-40 minutes to obtain a mixed solution, and placing the mixed solution in a 42°C water bath to heat shock After 45 s, cooling on ice for 2 min gave the conversion product.

具体地,所述载体为pYLXP’。Specifically, the vector is pYLXP'.

具体地,将所述转化子进行PCR扩增验证,将验证正确的所述转化子转入所述解脂耶氏酵母感受态细胞中。Specifically, the transformants are verified by PCR amplification, and the verified transformants are transferred into the Yarrowia lipolytica competent cells.

再一方面,本发明实施例提供了一种如上所述的真核工程菌株的应用,所述应用包括:将所述真核工程菌株转接于酵母浸出粉胨葡萄糖培养基中进行传代培养,经过三次传代培养,得到第三代真核菌株,将所述第三代真核菌株转接于酵母菌完全补充混合培养基上,将所述第三代真核菌株转接于酵母菌完全补充混合培养基上,得到工程菌株,将所述工程菌株经过发酵培养用于合成乙酰化甘油三酯。In another aspect, the embodiment of the present invention provides an application of the above-mentioned eukaryotic engineering strain, the application comprising: transferring the eukaryotic engineering strain into a yeast extract peptone glucose medium for subculture, After three subcultures, a third-generation eukaryotic strain is obtained, and the third-generation eukaryotic strain is transferred to a yeast-completely supplemented mixed medium, and the third-generation eukaryotic strain is transferred to a yeast-completely complemented mixed medium. On the mixed medium, an engineered strain is obtained, and the engineered strain is fermented and cultured for synthesizing acetylated triglycerides.

具体地,所述发酵培养的温度为28℃,所述发酵培养的时间为48h。Specifically, the temperature of the fermentation culture is 28°C, and the time of the fermentation culture is 48h.

具体地,所述真核工程菌株在于200~250rpm的转速下发酵培养。Specifically, the eukaryotic engineering strain is fermented and cultured at a rotational speed of 200-250 rpm.

本发明实施例提供的技术方案带来的有益效果是:本发明实施例提供了一种真核工程菌株及其制备方法和应用,该真核工程菌株能够大量合成乙酰化甘油三酯,可以通该真核工程菌株实现乙酰化甘油三酯的大规模生产,本发明实施例提供的制备方法能够获得大量的真核工程菌株,为乙酰化甘油三酯进行大规模生产提供基础,该应用包括将该真核工程菌株用于合成乙酰化甘油三酯。The beneficial effects brought by the technical solutions provided in the embodiments of the present invention are as follows: the embodiments of the present invention provide a eukaryotic engineering strain and a preparation method and application thereof. The eukaryotic engineering strain can synthesize a large amount of acetylated triglycerides, and can pass The eukaryotic engineering strain realizes large-scale production of acetylated triglycerides, and the preparation method provided in the embodiment of the present invention can obtain a large number of eukaryotic engineering strains, which provides a basis for the large-scale production of acetylated triglycerides. This eukaryotic engineering strain is used to synthesize acetylated triglycerides.

附图说明Description of drawings

为了更清楚地说明本发明实施例中的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to illustrate the technical solutions in the embodiments of the present invention more clearly, the following briefly introduces the accompanying drawings used in the description of the embodiments. Obviously, the accompanying drawings in the following description are only some embodiments of the present invention. For those of ordinary skill in the art, other drawings can also be obtained from these drawings without creative effort.

图1是本发明实施例提供的扩增产物的琼脂糖凝胶电泳图;Fig. 1 is the agarose gel electrophoresis figure of the amplification product provided in the embodiment of the present invention;

图2是本发明实施例提供的验证扩增产物的琼脂糖凝胶电泳图;Fig. 2 is the agarose gel electrophoresis figure of the verification amplification product provided in the embodiment of the present invention;

图3是本发明实施例提供的酶切产物的琼脂糖凝胶电泳图;Fig. 3 is the agarose gel electrophoresis figure of the enzyme cleavage product provided in the embodiment of the present invention;

图4是本发明实施例提供的硅胶板上脂质分布情况图。FIG. 4 is a graph of lipid distribution on a silica gel plate provided in an embodiment of the present invention.

具体实施方式Detailed ways

为使本发明的目的、技术方案和优点更加清楚,下面将结合附图对本发明实施方式作进一步地详细描述。In order to make the objectives, technical solutions and advantages of the present invention clearer, the embodiments of the present invention will be further described in detail below with reference to the accompanying drawings.

实施例Example

本发明实施例提供了一种真核工程菌株,该真核工程菌株表达的蛋白为甘油二酯乙酰化转移酶(Diacylglycerol Acetyltransferase,DAcT),甘油二酯乙酰化转移酶的氨基酸序列表中SEQ ID NO:1所示,该甘油二酯乙酰化转移酶源自扶芳藤。The embodiment of the present invention provides a eukaryotic engineering strain, the protein expressed by the eukaryotic engineering strain is diacylglycerol acetyltransferase (Diacylglycerol Acetyltransferase, DAcT), and SEQ ID in the amino acid sequence table of diacylglycerol acetyltransferase NO: 1 shows that the diacylglycerol acetyltransferase is derived from Fu Fang.

本发明实施例提供了一种真核工程菌株的制备方法,该制备方法包括:The embodiment of the present invention provides a preparation method of a eukaryotic engineering strain, and the preparation method includes:

根据解脂耶氏酵母的密码子偏好性来优化植物来源甘油二酯乙酰化转移酶编码基因EfDAcT。The gene EfDAcT encoding a plant-derived diglyceride acetyltransferase was optimized according to the codon preference of Yarrowia lipolytica.

将经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT的质粒与载体连接,得到连接产物pYLXP’::EfDAcT。其中,经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT的质粒的核苷酸序列如序列表中SEQ ID NO:4所示。The codon-optimized plasmid of the diacylglycerol acetyltransferase encoding gene EfDAcT was ligated with the vector to obtain the ligation product pYLXP'::EfDAcT. Wherein, the nucleotide sequence of the plasmid of the codon-optimized diglyceride acetyltransferase encoding gene EfDAcT is shown in SEQ ID NO: 4 in the sequence listing.

在实现时,经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT由中国农业科学院提供。经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT的具体制备方法包括:以化学合成的EfDAcT基因序列作为cDNA模板,利用正向引物EfDAcT-F和反向引物EfDAcT-R进行PCR扩增,该扩增产物即为经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT。其中,正向引物的序列如序列表中SEQ ID NO:2所示,反向引物的序列如序列表中SEQ ID NO:3所示。该PCR扩增体系共25μL,且该PCR扩增体系如表1所示。At the time of implementation, the codon-optimized diglyceride acetyltransferase encoding gene EfDAcT was provided by the Chinese Academy of Agricultural Sciences. The specific preparation method of the codon-optimized diglyceride acetyltransferase encoding gene EfDAcT includes: using the chemically synthesized EfDAcT gene sequence as a cDNA template, using forward primer EfDAcT-F and reverse primer EfDAcT-R to carry out PCR amplification , the amplification product is the codon-optimized diacylglycerol acetyltransferase encoding gene EfDAcT. The sequence of the forward primer is shown in SEQ ID NO: 2 in the sequence listing, and the sequence of the reverse primer is shown in SEQ ID NO: 3 in the sequence listing. The PCR amplification system is 25 μL in total, and the PCR amplification system is shown in Table 1.

表1为PCR扩增体系Table 1 shows the PCR amplification system

Figure BDA0002214857340000041
Figure BDA0002214857340000041

PCR扩增程序如下:The PCR amplification procedure is as follows:

Figure BDA0002214857340000042
Figure BDA0002214857340000042

将扩增产物采用浓度为1%的琼脂糖凝胶电泳进行检测,电泳结果如图1所示,由图1可知,该电泳检测结果与实际一致,即扩增产物正确,且为经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT。利用胶回收试剂盒(购置于北京擎科新业生物技术有限公司)回收目的基因片段(扩增产物)。The amplification product was detected by agarose gel electrophoresis with a concentration of 1%. The electrophoresis result is shown in Figure 1. It can be seen from Figure 1 that the electrophoresis detection result is consistent with the actual situation, that is, the amplification product is correct, and the codon is passed through. The optimized diglyceride acetyltransferase encoding gene EfDAcT. The target gene fragment (amplification product) was recovered by using a gel recovery kit (purchased from Beijing Qingke Xinye Biotechnology Co., Ltd.).

将目的基因片段与载体连接,得到连接产物。在本实施例中,载体可以为pYLXP’,连接时可采用T4-DNA连接酶(购于New England Biolabs)。The target gene fragment is ligated with the vector to obtain the ligated product. In this embodiment, the vector can be pYLXP', and T4-DNA ligase (purchased from New England Biolabs) can be used for ligation.

将连接产物转入感受态细胞中,得到第一转化产物。该感受态细胞可以为大肠杆菌DH5α感受态细胞(购于南京诺唯赞公司)。在实现时,采用热击法将连接产物转入大肠杆菌DH5α感受态细胞中。具体地,在超净工作台上,取已经准备好的大肠杆菌DH5α感受态细胞的菌液,加入连接产物,轻轻摇匀,置于冰上30min左右。在已经准备好的42℃恒温水浴锅中热击45s,迅速在冰上冷却2min,得到第一转化产物。The ligation product is transformed into competent cells to obtain the first transformation product. The competent cells can be Escherichia coli DH5α competent cells (purchased from Nanjing Novozymes). When realized, the ligation product was transferred into E. coli DH5α competent cells by heat shock method. Specifically, on the ultra-clean workbench, take the prepared bacterial solution of Escherichia coli DH5α competent cells, add the ligation product, shake gently, and place on ice for about 30 minutes. Heat shock for 45s in the prepared 42°C constant temperature water bath, and quickly cool on ice for 2min to obtain the first transformation product.

将第一转化产物于37℃下发酵培养0.6~1h,得到第一复苏液;具体地,将第一转化产物培养于1mL的LB液体无抗性培养基中,于37℃摇床复苏1h左右。其中,LB液体无抗性培养基的制备方法包括:取5g进口酵母提取物、10g进口蛋白胨、10g无水氯化钠和1L无菌水混匀后,经121℃灭菌20min后使用。The first transformation product was fermented and cultured at 37°C for 0.6 to 1 hour to obtain the first recovery solution; specifically, the first transformation product was cultured in 1 mL of LB liquid resistance-free medium, and recovered in a shaker at 37°C for about 1 hour. . Among them, the preparation method of LB liquid resistance-free medium includes: taking 5g of imported yeast extract, 10g of imported peptone, 10g of anhydrous sodium chloride and 1L of sterile water, mixing, and sterilizing at 121°C for 20min before use.

将200μL第一复苏液涂布在含氨苄青霉素抗性的LB固体培养基上,把涂好的LB固体平板培养基的正面朝上放置20min,待第一复苏液完全被含氨苄青霉素抗性的LB固体平板培养基吸收后,将其倒置,于37℃的恒温培养箱中培养8~12h,得到转化子。该1L的含氨苄青霉素抗性的LB固体平板培养基的制备方法包括:称取5g进口氨苄青霉素粉末(购于BioSharp公司)溶解于100mL去离子水中,使其终浓度为50mg/mL,用规格为0.22μm的抽滤器进行无菌抽滤,将抽滤产物分装至灭菌的EP管中,于-20℃条件下保存。Coat 200 μL of the first resuscitation solution on the ampicillin-resistant LB solid medium, and place the coated LB solid plate medium face up for 20 minutes. After the LB solid plate medium was absorbed, it was inverted and cultured in a constant temperature incubator at 37°C for 8 to 12 hours to obtain transformants. The preparation method of the 1 L ampicillin-resistant LB solid plate medium comprises: weighing 5 g of imported ampicillin powder (purchased from BioSharp Company) and dissolving it in 100 mL of deionized water, so that the final concentration is 50 mg/mL. Sterile suction filtration was performed on a 0.22 μm suction filter, and the suction filtration product was divided into sterilized EP tubes and stored at -20°C.

将获得的转化子进行PCR扩增验证。该PCR扩增验证体系共25μL,且该PCR扩增验证体系如表2所示。The obtained transformants were verified by PCR amplification. The PCR amplification verification system is 25 μL in total, and the PCR amplification verification system is shown in Table 2.

表2为PCR扩增验证体系Table 2 is the PCR amplification verification system

Figure BDA0002214857340000051
Figure BDA0002214857340000051

PCR扩增程序如下:The PCR amplification procedure is as follows:

Figure BDA0002214857340000061
Figure BDA0002214857340000061

将验证扩增产物采用浓度为1%的琼脂糖凝胶电泳检测,电泳结果如图2所示,由图2可知,该电泳检测结果与实际一致。The verification amplification product is detected by agarose gel electrophoresis with a concentration of 1%. The electrophoresis result is shown in FIG. 2 . It can be seen from FIG. 2 that the electrophoresis detection result is consistent with the actual situation.

活化含连接产物的大肠杆菌DH5α菌株,并提取质粒,将质粒进行酶切,回收酶切产物。该酶切体系共30μL,且该酶切体系如表3所示。The Escherichia coli DH5α strain containing the ligation product was activated, and the plasmid was extracted, and the plasmid was digested to recover the digested product. The enzyme digestion system is 30 μL in total, and the enzyme digestion system is shown in Table 3.

表3为酶切体系Table 3 is the enzyme digestion system

Figure BDA0002214857340000062
Figure BDA0002214857340000062

将酶切产物采用浓度为1%的琼脂糖凝胶电泳检测,电泳结果如图3所示,由图3可知,该电泳检测结果与实际一致。利用胶回收试剂盒(购置于北京擎科新业生物技术有限公司)回收目的基因片段(酶切产物)。The enzyme cleavage product was detected by agarose gel electrophoresis with a concentration of 1%, and the electrophoresis result was shown in Fig. 3. It can be seen from Fig. 3 that the electrophoresis detection result was consistent with the actual situation. The target gene fragment (enzyme digestion product) was recovered using a gel recovery kit (purchased from Beijing Qingke Xinye Biotechnology Co., Ltd.).

将酶切产物转入解脂耶氏酵母感受态细胞中,得到第二转化产物;其中,解脂耶氏酵母感受态细胞的制备方法如下:The enzyme cleavage product is transferred into the Yarrowia lipolytica competent cell to obtain the second transformation product; wherein, the preparation method of the Yarrowia lipolytica competent cell is as follows:

1、宿主解脂耶氏酵母Po1g的培养1. Culture of host Yarrowia lipolytica Po1g

在本实施例中,感受态细胞由解脂耶氏酵母Po1g制备,该解脂耶氏酵母Po1g由中国农业科学院油料作物研究所应用微生物实验室保存提供。挑取新活化的解脂耶氏酵母Po1g的单一菌落,用牙签接种于2mL的酵母浸出粉胨葡萄糖液体培养基(YPD液体培养基)中,于28℃下恒温200rpm摇床培养12h,培养至解脂耶氏酵母Po1g的菌株生长到对数生长期的后期,得到菌悬液。将200μL的菌悬液接种于酵母浸出粉胨葡萄糖固体培养基(YPD固体培养基)中,于28℃培养22h,得到复苏后的解脂耶氏酵母Po1g。其中,YPD液体培养基的制备方法为:取10g进口酵母提取物、20g进口蛋白胨、20g葡萄糖和1L无菌水混匀后,经121℃灭菌20min后使用。In this example, competent cells were prepared from Yarrowia lipolytica Po1g, which was preserved and provided by the Laboratory of Applied Microbiology, Oil Crops Research Institute, Chinese Academy of Agricultural Sciences. Pick a single colony of newly activated Yarrowia lipolytica Po1g, inoculate it with a toothpick in 2 mL of yeast extract powder peptone glucose liquid medium (YPD liquid medium), and cultivate at 28 °C for 12 h on a shaker at a constant temperature of 200 rpm. The strain of Yarrowia lipolytica Po1g was grown to the late logarithmic growth phase to obtain a bacterial suspension. 200 μL of bacterial suspension was inoculated into yeast extract powder peptone glucose solid medium (YPD solid medium), and cultured at 28° C. for 22 h to obtain the recovered Yarrowia lipolytica Po1g. Among them, the preparation method of YPD liquid culture medium is as follows: take 10 g of imported yeast extract, 20 g of imported peptone, 20 g of glucose and 1 L of sterile water, mix well, and sterilize at 121°C for 20 minutes before use.

2、采用醋酸锂法制备解脂耶氏酵母Po1g感受态细胞2. Preparation of Yarrowia lipolytica Po1g competent cells by lithium acetate method

将复苏后的解脂耶氏酵母Po1g转入1.5mL无菌的EP管中,加入经过100℃处理的鲑鱼精5μL、90μL浓度为50%的PEG6000和5μL浓度为2mol/L的醋酸锂混合均匀,得到解脂耶氏酵母Po1g感受态细胞,得到的解脂耶氏酵母Po1g感受态细胞的菌液可直接用作宿主菌进行转化实验。Transfer the recovered Yarrowia lipolytica Po1g into a 1.5mL sterile EP tube, add 5 μL of salmon essence treated at 100°C, 90 μL of PEG6000 with a concentration of 50% and 5 μL of lithium acetate with a concentration of 2 mol/L and mix well. , to obtain Yarrowia lipolytica Po1g competent cells, and the obtained bacterial liquid of Yarrowia lipolytica Po1g competent cells can be directly used as host bacteria for transformation experiments.

采用热击法将酶切产物转入解脂耶氏酵母Po1g感受态细胞中,得到第二转化产物。具体地,在超净工作台上,取已经准备好的解脂耶氏酵母Po1g感受态细胞的菌液,加入酶切产物,轻轻摇匀。在已经准备好的39℃恒温水浴锅中热击30min,每隔10min进行混匀,得到第二转化产物。The enzyme-digested product was transformed into Yarrowia lipolytica Po1g competent cells by heat shock method to obtain the second transformation product. Specifically, on the ultra-clean workbench, take the prepared bacterial solution of Yarrowia lipolytica Po1g competent cells, add the enzyme digestion product, and shake gently. Heat shock for 30min in the prepared 39°C constant temperature water bath, and mix evenly every 10min to obtain the second conversion product.

将第二转化产物培养于1mL的YPD液体培养基中,于28℃摇床复苏1h左右,得到复苏液。The second transformation product was cultured in 1 mL of YPD liquid medium, and recovered in a shaker at 28° C. for about 1 hour to obtain a recovery solution.

将复苏液全部涂布在酵母菌完全补充混合培养基(CSM固体培养基)上,于37℃下培养12h,得到含目的基因的菌株,其中,CSM固体培养基的制备方法为:取0.69gCSM-Leu、1.7gYNB、20g葡萄糖、5g硫酸铵、10g琼脂粉和1L无菌水混匀后,经121℃灭菌20min后使用。All the resuscitation liquid was coated on the yeast complete supplemented mixed medium (CSM solid medium), and cultured at 37°C for 12 hours to obtain a strain containing the target gene. The preparation method of the CSM solid medium was as follows: take 0.69 g of CSM -Leu, 1.7g YNB, 20g glucose, 5g ammonium sulfate, 10g agar powder and 1L sterile water were mixed, sterilized at 121℃ for 20min before use.

在CSM固体培养基上长出的转化子单菌落作为真核工程菌株。Single colonies of transformants grown on CSM solid medium were used as eukaryotic engineering strains.

在实现时,可将真核工程菌株转接于YPD固体培养基长,进行三次传代培养,得到第三代真核菌株,将第三代真核菌株转接于CSM培养基中,得到工程菌株(Yarrowialipolytica/pYLXP’::EfDAcT),工程菌株用于合成乙酰化甘油三酯。When realized, the eukaryotic engineering strain can be transferred to YPD solid medium for three subcultures to obtain the third-generation eukaryotic strain, and the third-generation eukaryotic strain can be transferred to the CSM medium to obtain the engineered strain (Yarrowialipolytica/pYLXP'::EfDAcT), the engineered strain was used to synthesize acetylated triglycerides.

将工程菌株经过发酵培养合成乙酰化甘油三酯,在220rpm的转速下经摇床发酵培养,发酵培养基为YPD培养基,发酵培养的温度为28℃,发酵培养的时间为48h。The engineered strains were fermented and cultured to synthesize acetylated triglycerides, which were fermented and cultured in a shaker at a rotational speed of 220 rpm. The fermentation medium was YPD medium, the temperature of fermentation was 28°C, and the time of fermentation was 48h.

检测工程菌株合成的乙酰化甘油三酯。Detection of acetylated triglycerides synthesized by engineered strains.

发酵结束后,将菌液转移至50mL离心管中,于6000rpm离心8min,并收集沉淀物(菌体),将菌体放置于-80℃的超低温冰箱预冷12h。将预冷后的菌体放在真空冷冻干燥机中干燥24h,称重。用研钵将菌体研磨至粉末状,得到菌粉,称取2mg菌粉,并转移至4mL螺纹玻璃瓶中,向螺纹玻璃瓶中依次加入1mL甲醇、1mL氯仿、10μL浓度为0.5mg/mL的十五烷酸甘油三酯标品和20μL浓度为1mg/mL的十五烷酸标品,将螺纹玻璃瓶超声振荡15min,使得菌粉和试剂充分互溶。然后在低速离心机中以3500rpm的速率离心10min,再以4000rpm离心5min,得到上清液(待测样品),小心地将上清液转移至新的4mL螺纹玻璃瓶中,并于-20℃保存。After the fermentation, the bacterial liquid was transferred to a 50 mL centrifuge tube, centrifuged at 6000 rpm for 8 min, and the sediment (cell) was collected, and the cell was placed in an ultra-low temperature refrigerator at -80 °C for 12 h. The pre-cooled cells were dried in a vacuum freeze dryer for 24 h and weighed. Grind the bacterial cells into powder with a mortar to obtain bacterial powder, weigh 2 mg of bacterial powder, and transfer it to a 4 mL threaded glass bottle. Add 1 mL of methanol, 1 mL of chloroform, and 10 μL to the threaded glass bottle in sequence to a concentration of 0.5 mg/mL. The standard pentadecanoic acid triglyceride and 20 μL of the standard pentadecanoic acid with a concentration of 1 mg/mL were ultrasonically shaken for 15 min in the screw glass bottle, so that the bacteria powder and the reagent were fully dissolved in each other. Then centrifuge at 3500rpm for 10min in a low-speed centrifuge, and then centrifuge at 4000rpm for 5min to obtain the supernatant (sample to be tested). save.

采用薄层层析(Thin-layer chromatography,TLC)分离不同种类的油脂并进行分析,具体方法如下:Thin-layer chromatography (TLC) was used to separate and analyze different types of oils and fats. The specific methods are as follows:

1、配置TLC层析剂:在通风橱中配制TLC层析剂,TLC层析剂包括体积比为70:30:1的色谱级正己烷、分析纯乙醚和分析纯乙酸,正己烷、乙醚和乙酸,将配制好的TLC层析剂后摇匀。1. Prepare TLC chromatography agent: prepare TLC chromatography agent in a fume hood. TLC chromatography agent includes chromatographic grade n-hexane with a volume ratio of 70:30:1, analytically pure ether and analytically pure acetic acid, n-hexane, ether and acetic acid, and shake the prepared TLC chromatography agent.

2、点样:在硅胶板(Silica gel 60,20×20cm;EMD Chemicals,Germany)的一侧距边沿1.5cm处用铅笔画一条水平直线,按照一定的间隔在直线上标记所要点的待测样品。吹干后的待测样品用100μL色谱级氯仿复溶,在硅胶板相应的标记处点样,重复一次操作,点样时尽量保证每个点的直径尽可能小。2. Spotting: Draw a horizontal straight line with a pencil at a distance of 1.5 cm from the edge on one side of the silica gel plate (Silica gel 60, 20×20 cm; EMD Chemicals, Germany), and mark the samples to be tested on the straight line at certain intervals. . After drying, the sample to be tested was reconstituted with 100 μL of chromatographic grade chloroform, and the sample was spotted at the corresponding mark on the silica gel plate.

3、在点样结束前约10min,将配置好的TLC层析剂倒入层析缸内。点完样品后,将硅胶板置于展层缸中,进行展开。当TLC层析剂跑至距硅胶板上沿约1cm时,取出硅胶板在通风橱中晾干。3. About 10 minutes before the end of sampling, pour the configured TLC chromatography agent into the chromatography cylinder. After spotting the sample, place the silica gel plate in the layer cylinder for development. When the TLC chromatography agent runs to about 1 cm from the edge of the silica gel plate, take out the silica gel plate and dry it in a fume hood.

4、显色。将丙酮和水按照体积比为4:1进行混合,得到混合液,称取10mgprimuline溶于20mL混合液中制成显色液,将显色液均匀并喷在硅胶板的表面进行显色。在紫外灯下观察硅胶板上脂质分布情况,并拍照留存结果,其结果如图4所示,由图4可见乙酰化甘油三酯(AcTAG)条带、甘油三酯(TAG)条带、游离脂肪酸(FFA)条带、甘油二酯(DAG)和甘油单酯(MAG)条带。将其中的乙酰化甘油三酯条带刮下来进行甲脂化,得到甲酯化的乙酰化甘油三酯。4. Color rendering. Mix acetone and water at a volume ratio of 4:1 to obtain a mixed solution. Weigh 10 mg of primuline and dissolve it in 20 mL of mixed solution to prepare a color developing solution. The color developing solution is uniformly sprayed on the surface of the silica gel plate for color development. The lipid distribution on the silica gel plate was observed under UV light, and the results were photographed. The results are shown in Figure 4. From Figure 4, acetylated triglyceride (AcTAG) bands, Free fatty acid (FFA), diglyceride (DAG) and monoglyceride (MAG) bands. The acetylated triglyceride strip is scraped off for methyl esterification to obtain methyl esterified acetylated triglyceride.

将乙酰化甘油三酯进行气相定量分析:Gas-phase quantitative analysis of acetylated triglycerides:

将经过甲酯化的乙酰化甘油三酯转移至4mL螺纹透明玻璃瓶中,向螺纹透明玻璃瓶中加入0.75mL硫酸甲醇(硫酸甲醇中的硫酸与甲醇的体积比为5:95),将螺纹透明玻璃瓶的瓶盖密封后振荡混匀。将螺纹透明玻璃瓶置于92℃水浴锅中进行水浴,水浴时间1.5h。待螺纹透明玻璃瓶冷却至室温以后,向螺纹透明玻璃瓶中加入500μL浓度为0.9%的NaCl溶液和300μL色谱级正己烷,经过涡旋振荡1min,于3500rpm离心20min,得到上层溶液(有机相),取上层溶液转移至1.5mL的EP管中,于12000rpm离心10min,得到上清液,将上清液转移至GC瓶中,采用气相色谱检测产物中的脂肪酸组成。The methylated acetylated triglyceride was transferred to a 4mL thread transparent glass bottle, 0.75mL sulfuric acid methanol (the volume ratio of sulfuric acid and methanol in sulfuric acid methanol was 5:95) was added to the thread transparent glass bottle, and the thread The cap of the transparent glass bottle was sealed and mixed by shaking. The threaded transparent glass bottle was placed in a water bath at 92°C for a water bath, and the water bath time was 1.5h. After the threaded transparent glass bottle was cooled to room temperature, 500 μL of 0.9% NaCl solution and 300 μL of chromatographic grade n-hexane were added to the threaded transparent glass bottle, vortexed for 1 min, and centrifuged at 3500 rpm for 20 min to obtain the upper layer solution (organic phase) , transfer the upper layer solution to a 1.5mL EP tube, centrifuge at 12000rpm for 10min to obtain a supernatant, transfer the supernatant to a GC bottle, and use gas chromatography to detect the fatty acid composition in the product.

本实施例采用安捷伦7890A气相色谱仪来检测脂肪酸甲酯化样品,色谱条件如下:The present embodiment adopts Agilent 7890A gas chromatograph to detect fatty acid methylation samples, and the chromatographic conditions are as follows:

分离脂肪酸甲酯采用的色谱柱为HP-FFAP(30m×250μm×0.25μm),氢离子火焰化检测器(Flame Ionization Detector,FID);载气为纯度99.999%的氮气;按程序升温:最初开始温度,150℃,10℃/min升高温度至210℃,保持7min;继续以20℃/min升高温度至230℃,保持6min;分流比为30:1;进样口温度为260℃。The chromatographic column used for the separation of fatty acid methyl esters is HP-FFAP (30m×250μm×0.25μm), and a flame ionization detector (FID); the carrier gas is nitrogen with a purity of 99.999%; the temperature is programmed according to the initial start Temperature, 150°C, 10°C/min increase the temperature to 210°C, hold for 7min; continue to increase the temperature at 20°C/min to 230°C, hold for 6min; the split ratio is 30:1; the injection port temperature is 260°C.

经检测,每克工程菌株样品中的乙酰化甘油三酯的量为30mg,乙酰化甘油三酯的量占每克工程菌株干重的比例为3%,乙酰化甘油三酯的量占总甘油三酯的比例为18%。由此可见,通过该工程菌株获得的乙酰化甘油三酯具有较高的含量。After testing, the amount of acetylated triglycerides in each gram of engineering strain samples was 30 mg, the proportion of acetylated triglycerides in the dry weight of each gram of engineering strains was 3%, and the amount of acetylated triglycerides accounted for the total glycerol. The proportion of triesters was 18%. It can be seen that the acetylated triglyceride obtained by this engineering strain has a higher content.

本发明实施例提供了一种真核工程菌株及其制备方法和应用,该真核工程菌株能够大量合成乙酰化甘油三酯,可以通该真核工程菌株实现乙酰化甘油三酯的大规模生产,本发明实施例提供的制备方法能够获得大量的真核工程菌株,为乙酰化甘油三酯进行大规模生产提供基础,该应用包括将该真核工程菌株用于合成乙酰化甘油三酯。The embodiment of the present invention provides a eukaryotic engineering strain and a preparation method and application thereof, the eukaryotic engineering strain can synthesize acetylated triglycerides in large quantities, and the large-scale production of acetylated triglycerides can be realized by the eukaryotic engineering strain , the preparation method provided in the embodiment of the present invention can obtain a large number of eukaryotic engineering strains, which provides a basis for the large-scale production of acetylated triglycerides. The application includes using the eukaryotic engineering strains to synthesize acetylated triglycerides.

以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the protection of the present invention. within the range.

序列表sequence listing

<110> 中国农业科学院油料作物研究所<110> Oil Crops Research Institute, Chinese Academy of Agricultural Sciences

<120> 一种真核工程菌株及其制备方法和应用<120> A kind of eukaryotic engineering strain and its preparation method and application

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<213> 人工序列(Artificial Sequence)<213> Artificial Sequence

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Met Met Asp Val His Gln Glu Ile Asn Asn Phe Ile Lys Val Trp ValMet Met Asp Val His Gln Glu Ile Asn Asn Phe Ile Lys Val Trp Val

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Leu Leu Ile Pro Pro Leu Asn Ile Ser Ser Phe Ile Leu Ser Ser IleLeu Leu Ile Pro Pro Leu Asn Ile Ser Ser Phe Ile Leu Ser Ser Ile

50 55 60 50 55 60

Thr Gly Phe Phe Leu Ala Trp Leu Thr Thr Phe Lys Val Ile Ser PheThr Gly Phe Phe Leu Ala Trp Leu Thr Thr Phe Lys Val Ile Ser Phe

65 70 75 8065 70 75 80

Ala Phe Asp Gln Gly Pro Leu Tyr Pro Leu Pro Gln Asn Leu Leu HisAla Phe Asp Gln Gly Pro Leu Tyr Pro Leu Pro Gln Asn Leu Leu His

85 90 95 85 90 95

Phe Ile Ser Ile Ala Cys Leu Pro Ile Thr Val Lys Arg Asn Pro SerPhe Ile Ser Ile Ala Cys Leu Pro Ile Thr Val Lys Arg Asn Pro Ser

100 105 110 100 105 110

Pro Lys Leu Lys Ser Thr Thr Asn Thr Ser Pro Ile Ser His Ile LeuPro Lys Leu Lys Ser Thr Thr Asn Thr Ser Pro Ile Ser His Ile Leu

115 120 125 115 120 125

Lys Ser Val Phe Met Ser Phe Pro Ser Lys Val Leu Leu His Trp IleLys Ser Val Phe Met Ser Phe Pro Ser Lys Val Leu Leu His Trp Ile

130 135 140 130 135 140

Ile Ala His Leu Tyr Gln Tyr Lys Lys Tyr Met Asp Pro Asn Val ValIle Ala His Leu Tyr Gln Tyr Lys Lys Tyr Met Asp Pro Asn Val Val

145 150 155 160145 150 155 160

Leu Val Ile Tyr Cys Cys His Val Tyr Val Leu Leu Asp Ile Ser LeuLeu Val Ile Tyr Cys Cys His Val Tyr Val Leu Leu Asp Ile Ser Leu

165 170 175 165 170 175

Ser Leu Cys Ala Thr Leu Ala Glu Phe Leu Cys Gly Phe Asp Val GluSer Leu Cys Ala Thr Leu Ala Glu Phe Leu Cys Gly Phe Asp Val Glu

180 185 190 180 185 190

Pro Gln Phe Lys Glu Pro Tyr Leu Ala Thr Ser Leu Gln Asp Phe TrpPro Gln Phe Lys Glu Pro Tyr Leu Ala Thr Ser Leu Gln Asp Phe Trp

195 200 205 195 200 205

Gly Arg Arg Trp Asn Ile Ile Val Ser Ser Val Leu Arg Ser Thr ValGly Arg Arg Trp Asn Ile Ile Val Ser Ser Val Leu Arg Ser Thr Val

210 215 220 210 215 220

Tyr Thr Pro Thr Arg His Ile Ala Ser Tyr Leu Ile Gly Ser Arg TrpTyr Thr Pro Thr Arg His Ile Ala Ser Tyr Leu Ile Gly Ser Arg Trp

225 230 235 240225 230 235 240

Ala Tyr Phe Pro Ala Ile Ile Ala Thr Phe Val Val Ser Gly Val MetAla Tyr Phe Pro Ala Ile Ile Ala Thr Phe Val Val Ser Gly Val Met

245 250 255 245 250 255

His Asp Ile Val Tyr Tyr Val Tyr Met Met His Val Tyr Pro Lys TrpHis Asp Ile Val Tyr Tyr Val Tyr Met Met His Val Tyr Pro Lys Trp

260 265 270 260 265 270

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275 280 285 275 280 285

Val Glu Met Lys Cys Lys Arg Ser Arg Arg Asp Lys Trp Arg Arg HisVal Glu Met Lys Cys Lys Arg Ser Arg Arg Asp Lys Trp Arg Arg His

290 295 300 290 295 300

Pro Val Val Asp Trp Val Met Val Met Gly Phe Val Met Gly Thr SerPro Val Val Asp Trp Val Met Val Met Gly Phe Val Met Gly Thr Ser

305 310 315 320305 310 315 320

Val Ser Leu Leu Phe Val Pro Leu Leu Arg Asp Asn Val Asp Gln IleVal Ser Leu Leu Phe Val Pro Leu Leu Arg Asp Asn Val Asp Gln Ile

325 330 335 325 330 335

Val Ala Glu Glu Cys Ser Ile Leu Leu Asn Phe Val Arg Glu Lys IleVal Ala Glu Glu Cys Ser Ile Leu Leu Asn Phe Val Arg Glu Glu Lys Ile

340 345 350 340 345 350

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355 360 355 360

<210> 2<210> 2

<211> 28<211> 28

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<213> 人工序列(Artificial Sequence)<213> Artificial Sequence

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cggaattcga tgatggacgt acaccagg 28cggaattcga tgatggacgt acaccagg 28

<210> 3<210> 3

<211> 29<211> 29

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<213> 人工序列(Artificial Sequence)<213> Artificial Sequence

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<210> 4<210> 4

<211> 1092<211> 1092

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<213> 人工序列(Artificial Sequence)<213> Artificial Sequence

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atgatggacg tgcaccaaga gatcaacaac ttcatcaagg tgtgggtgca agccatggcc 60atgatggacg tgcaccaaga gatcaacaac ttcatcaagg tgtgggtgca agccatggcc 60

tgcctgtctt acgcctacta cttctcttcg cgactgccca agggcctgct gcgactgctg 120tgcctgtctt acgcctacta cttctcttcg cgactgccca agggcctgct gcgactgctg 120

tctctgctgc ccgtgttcta cctgctgctg atccctcctc tgaacatctc ttctttcatc 180tctctgctgc ccgtgttcta cctgctgctg atccctcctc tgaacatctc ttctttcatc 180

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gccttcgacc agggacctct gtaccctctg cctcagaacc tgctgcactt catctctatc 300gccttcgacc agggacctct gtaccctctg cctcagaacc tgctgcactt catctctatc 300

gcctgtctgc ccatcaccgt gaagcgaaac ccctcgccta agctgaagtc taccaccaac 360gcctgtctgc ccatcaccgt gaagcgaaac ccctcgccta agctgaagtc taccaccaac 360

acttctccca tctctcacat cctgaagtct gtgttcatgt cgtttccctc gaaggtgctg 420acttctccca tctctcacat cctgaagtct gtgttcatgt cgtttccctc gaaggtgctg 420

ctgcattgga tcattgccca cctgtaccag tacaagaagt acatggaccc caacgtggtg 480ctgcattgga tcattgccca cctgtaccag tacaagaagt acatggaccc caacgtggtg 480

ctggtgatct actgctgtca cgtgtacgtg ctgctggaca tctctctgtc tctgtgcgct 540ctggtgatct actgctgtca cgtgtacgtg ctgctggaca tctctctgtc tctgtgcgct 540

accctggccg agttcctgtg cggcttcgac gttgagcccc agttcaagga accctacctg 600accctggccg agttcctgtg cggcttcgac gttgagcccc agttcaagga accctacctg 600

gctacctctc tgcaggactt ctggggccga cgatggaaca tcatcgtgtc ctccgtgctg 660gctacctctc tgcaggactt ctggggccga cgatggaaca tcatcgtgtc ctccgtgctg 660

cgatctaccg tgtacacccc tactcgacac attgcctctt acctgatcgg ctctcgatgg 720cgatctaccg tgtacacccc tactcgacac attgcctctt acctgatcgg ctctcgatgg 720

gcttacttcc ccgccattat cgccaccttc gtggtgtctg gcgtgatgca cgacatcgtg 780gcttacttcc ccgccattat cgccaccttc gtggtgtctg gcgtgatgca cgacatcgtg 780

tactacgtct acatgatgca cgtgtacccc aagtgggaca tgaccggcca cttcgtgctg 840tactacgtct acatgatgca cgtgtacccc aagtgggaca tgaccggcca cttcgtgctg 840

cacggcatct gcgaggccct cgaggtggaa atgaagtgta agcgatctcg acgagacaag 900cacggcatct gcgaggccct cgaggtggaa atgaagtgta agcgatctcg acgagacaag 900

tggcgacgac accccgtggt ggactgggtg atggtgatgg gattcgtgat gggaacctct 960tggcgacgac accccgtggt ggactgggtg atggtgatgg gattcgtgat gggaacctct 960

gtgtccctgc tgttcgtgcc tctgctgcga gacaacgtgg accagatcgt ggccgaggaa 1020gtgtccctgc tgttcgtgcc tctgctgcga gacaacgtgg accagatcgt ggccgaggaa 1020

tgctctatcc tgctgaactt cgtgcgagag aagatcgtga tgctgggcac ccgattcatc 1080tgctctatcc tgctgaactt cgtgcgagag aagatcgtga tgctgggcac ccgattcatc 1080

tgcggcaact aa 1092tgcggcaact aa 1092

Claims (10)

1.一种真核工程菌株,其特征在于,所述真核工程菌株表达的蛋白为甘油二酯乙酰化转移酶,所述甘油二酯乙酰化转移酶的氨基酸序列表中SEQ ID NO:1所示。1. a eukaryotic engineering strain, is characterized in that, the protein expressed by described eukaryotic engineering strain is diglyceride acetyltransferase, and SEQ ID NO:1 in the amino acid sequence table of described diglyceride acetyltransferase shown. 2.一种如根据权利要求1所述的真核工程菌株的制备方法,其特征在于,所述制备方法包括:2. a preparation method of eukaryotic engineering strain as claimed in claim 1, is characterized in that, described preparation method comprises: 将经过密码子优化的甘油二酯乙酰化转移酶编码基因EfDAcT与载体连接,得到连接产物;connecting the codon-optimized diglyceride acetyltransferase encoding gene EfDAcT with the carrier to obtain a ligated product; 将所述连接产物转入感受态细胞中,得到第一转化产物;transferring the ligation product into competent cells to obtain the first transformation product; 将所述第一转化产物于37℃下摇床培养0.6~1h,得到第一复苏液;The first transformation product is incubated at 37°C in a shaker for 0.6 to 1 hour to obtain a first resuscitation solution; 将所述第一复苏液涂布在含氨苄青霉素抗性的固体培养基上,于37℃下培养8~12h,得到转化子;Coating the first resuscitation solution on a solid medium containing ampicillin resistance, and culturing at 37°C for 8-12 hours to obtain transformants; 提取所述转化子的质粒,将所述质粒进行酶切,得到酶切产物;The plasmid of the transformant is extracted, and the plasmid is digested to obtain the digested product; 将所述酶切产物转入解脂耶氏酵母感受态细胞中,得到第二转化产物;Transferring the enzyme cleavage product into Yarrowia lipolytica competent cells to obtain a second transformation product; 将所述第二转化产物在酵母浸出粉胨葡萄糖液体培养基中于28℃下摇床培养0.6~1.2h,得到第二复苏液;The second transformation product is cultured in a yeast extract peptone glucose liquid medium at 28° C. in a shaker for 0.6-1.2 hours to obtain a second resuscitation solution; 将所述第二复苏液涂布在酵母菌完全补充混合培养基上,于37℃下培养8~12h,得到所述真核工程菌株。The second resuscitation solution is coated on the yeast complete supplemented mixed medium, and cultured at 37° C. for 8-12 hours to obtain the eukaryotic engineering strain. 3.根据权利要求2所述的制备方法,其特征在于,所述EfDAcT基因的制备方法包括:将合成的EfDAcT基因序列作为cDNA模板,利用上游引物和下游引物进行扩增,得到所述EfDAcT基因,所述上游引物的序列如序列表中SEQ ID NO:2所示,所述下游引物的序列如序列表中SEQ ID NO:3所示。3. preparation method according to claim 2, is characterized in that, the preparation method of described EfDAcT gene comprises: using synthetic EfDAcT gene sequence as cDNA template, utilize upstream primer and downstream primer to carry out amplification, obtain described EfDAcT gene , the sequence of the upstream primer is shown in SEQ ID NO: 2 in the sequence listing, and the sequence of the downstream primer is shown in SEQ ID NO: 3 in the sequence listing. 4.根据权利要求2所述的制备方法,其特征在于,采用热击法将所述连接产物转入所述感受态细胞中。4 . The preparation method according to claim 2 , wherein the ligation product is transferred into the competent cells by a heat shock method. 5 . 5.根据权利要求4所述的制备方法,其特征在于,所述热击法包括:将所述连接产物和所述感受态细胞混合后,置于冰上30~40min,得到混合液,将所述混合液置于42℃水浴锅中热击45s后,在冰上冷却2min,得到所述转化产物。5 . The preparation method according to claim 4 , wherein the thermal shock method comprises: after mixing the ligation product and the competent cells, placing it on ice for 30-40 min to obtain a mixed solution, The mixture was placed in a water bath at 42° C. for 45 s and then cooled on ice for 2 min to obtain the conversion product. 6.根据权利要求2所述的制备方法,其特征在于,所述载体为pYLXP’。6. The preparation method according to claim 2, wherein the carrier is pYLXP'. 7.根据权利要求2所述的制备方法,其特征在于,将所述转化子进行PCR扩增验证,将验证正确的所述转化子转入所述解脂耶氏酵母感受态细胞中。7 . The preparation method according to claim 2 , wherein the transformant is subjected to PCR amplification verification, and the verified transformant is transferred into the Yarrowia lipolytica competent cell. 8 . 8.一种如权利要求1所述的真核工程菌株的应用,其特征在于,所述应用包括:将所述真核工程菌株转接于酵母浸出粉胨葡萄糖培养基中进行传代培养,经过三次传代培养,得到第三代真核菌株,将所述第三代真核菌株转接于酵母菌完全补充混合培养基上,将所述第三代真核菌株转接于酵母菌完全补充混合培养基上,得到工程菌株,将所述工程菌株经过发酵培养用于合成乙酰化甘油三酯。8. the application of a eukaryotic engineering strain as claimed in claim 1, is characterized in that, described application comprises: described eukaryotic engineering strain is transferred in yeast leaching peptone glucose medium to carry out subculture, through Subculture for three times to obtain a third-generation eukaryotic strain, transfer the third-generation eukaryotic strain to a yeast complete supplemented mixed medium, and transfer the third-generation eukaryotic strain to a yeast complete complementary mixed medium On the medium, an engineered strain is obtained, and the engineered strain is fermented and cultured for synthesizing acetylated triglycerides. 9.根据权利要求8所述的应用,其特征在于,所述发酵培养的温度为28℃,所述发酵培养的时间为48h。9 . The application according to claim 8 , wherein the temperature of the fermentation culture is 28° C., and the time of the fermentation culture is 48 hours. 10 . 10.根据权利要求8所述的应用,其特征在于,所述工程菌株在于200~250rpm的转速下发酵培养。10 . The application according to claim 8 , wherein the engineered strain is fermented and cultured at a rotational speed of 200-250 rpm. 11 .
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