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CN103555646B - Genetic engineering bacterium for co-expressing L-arabinose isomerase gene and mannose-6-phosphate isomerase - Google Patents

Genetic engineering bacterium for co-expressing L-arabinose isomerase gene and mannose-6-phosphate isomerase Download PDF

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CN103555646B
CN103555646B CN201310519792.9A CN201310519792A CN103555646B CN 103555646 B CN103555646 B CN 103555646B CN 201310519792 A CN201310519792 A CN 201310519792A CN 103555646 B CN103555646 B CN 103555646B
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徐虹
詹伊婧
徐铮
李莎
冯小海
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Nanjing Tech University
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Abstract

本发明公开了一种共表达L‑阿拉伯糖异构酶基因和甘露糖‑6‑磷酸异构酶的基因工程菌。该菌株包含SEQ ID NO:1和SEQ ID NO:2所示的核苷酸序列。本发明的基因工程菌可以通过催化L‑阿拉伯糖生产L‑核糖,一步转化,工艺简单,转化率高,通过本发明的基因工程菌,L‑核糖的转化率达到25~50%,具有良好的产业化前景。The invention discloses a genetic engineering bacterium co-expressing L-arabinose isomerase gene and mannose-6-phosphate isomerase. The strain contains the nucleotide sequences shown in SEQ ID NO:1 and SEQ ID NO:2. The genetically engineered bacterium of the present invention can produce L-ribose by catalyzing L-arabinose, one-step conversion, process is simple, and conversion rate is high, through the genetically engineered bacterium of the present invention, the conversion rate of L-ribose reaches 25~50%, has good industrialization prospects.

Description

一种共表达L-阿拉伯糖异构酶基因和甘露糖-6-磷酸异构酶 的基因工程菌A co-expression of L-arabinose isomerase gene and mannose-6-phosphate isomerase genetically engineered bacteria

技术领域technical field

本发明属于生物工程技术领域,具体涉及一种共表达L-阿拉伯糖异构酶基因和甘露糖-6-磷酸异构酶基因的基因工程菌构建及其应用。The invention belongs to the technical field of bioengineering, and in particular relates to the construction and application of a genetic engineering bacterium co-expressing L-arabinose isomerase gene and mannose-6-phosphate isomerase gene.

背景技术Background technique

核糖(Ribose,C5H10O5)是一种典型的五碳糖,是各种核糖核酸(RNA)、核苷酸辅酶、以及ATP、NADP的组成成分,与生物遗传的关系密切,对生物体的生理活性具有重要的调控作用。自然界中的核糖主要以D-核糖形态存在,D-核糖以呋喃糖型广泛存在于植物和动物细胞中,D-核糖也是多种维生素、辅酶以及某些抗生素,如新霉素A、B和巴龙霉素的成分;L-核糖是与D-核糖相对的手性对映异构体,在自然界和生物体内并不存在,是极为昂贵的稀有糖类。纯净的L-核糖是白色晶体或白色晶体粉末,带有甜味;可溶于水、乙醇、甲醇、不溶于乙醚、苯和丙酮。L-核糖具有良好的抗肿瘤抗病毒能力且对正常细胞的毒副作用很小。L-核糖是重要的药物合成中间体,广泛用于合成具有抗病毒活性的核苷类化合物,在抗艾滋病、抗病毒中间体方面显示强大的潜能。L-核糖经还原脱氧水解等加工还可生产2-脱氧-L-核糖,该中间体与腺嘌呤等有机碱形成的核苷衍生物在癌症、乙肝、丙肝等疾病的治疗方面也具有很大的应用潜能。Ribose (Ribose, C 5 H 10 O 5 ) is a typical five-carbon sugar, which is a component of various ribonucleic acid (RNA), nucleotide coenzymes, ATP, and NADP, and is closely related to biological genetics. The physiological activity of organisms plays an important role in regulation. Ribose in nature mainly exists in the form of D-ribose, which widely exists in plant and animal cells in the form of furanose. D-ribose is also a variety of vitamins, coenzymes and certain antibiotics, such as neomycin A, B and The composition of paromomycin; L-ribose is the chiral enantiomer opposite to D-ribose, which does not exist in nature and organisms, and is an extremely expensive rare sugar. Pure L-ribose is white crystal or white crystal powder with sweet taste; soluble in water, ethanol, methanol, insoluble in ether, benzene and acetone. L-ribose has good anti-tumor and anti-virus capabilities and has little toxic side effects on normal cells. L-ribose is an important drug synthesis intermediate, widely used in the synthesis of nucleoside compounds with antiviral activity, and has shown strong potential in anti-AIDS and antiviral intermediates. L-ribose can also produce 2-deoxy-L-ribose through reductive deoxyhydrolysis and other processing. The nucleoside derivatives formed by this intermediate and organic bases such as adenine also have great potential in the treatment of cancer, hepatitis B, hepatitis C and other diseases. application potential.

随着L-核糖应用面的不断扩大,全球L-核糖的需求量逐年增加,人们对制备和开发适应工业化生产L-核糖方法的兴趣日益浓厚。随着L-核糖应用面的不断扩大,全球L-核糖的需求量逐年增加,人们对制备和开发适应工业化生产L-核糖方法的兴趣日益浓厚。With the continuous expansion of the application of L-ribose, the global demand for L-ribose is increasing year by year, and people are increasingly interested in the preparation and development of methods suitable for industrial production of L-ribose. With the continuous expansion of the application of L-ribose, the global demand for L-ribose is increasing year by year, and people are increasingly interested in the preparation and development of methods suitable for industrial production of L-ribose.

尽管目前采用化学法合成L-核糖,在合成步骤与收率等方面均有了较大的提高,但仍存在合成工艺路线复杂,反应步骤繁琐,试剂昂贵,总收率低,需使用大量有机溶剂和产生有害的副产物等问题,难以适应工业化生产的要求。通过微生物或酶进行生物转化生产L-核糖已成为国内外研究热点,生物转化合成L-核糖具有立体选择性好、反应条件温和、污染少等特点。根据原料不同可分为两类:以核糖醇为原料和以L-阿拉伯糖为原料,其中值得提到的是近年来研究较多的以L-阿拉伯糖为原料转化为L-核糖需要 二步催化,很多研究人员致力于将L-阿拉伯糖异构酶和甘露糖-6-磷酸异构酶两种酶作为一个酶催化体系,实现两种酶一步催化L-阿拉伯糖生产L-核糖。Although the chemical synthesis of L-ribose has been greatly improved in terms of synthesis steps and yields, there are still complex synthetic process routes, cumbersome reaction steps, expensive reagents, low overall yields, and the need to use a large amount of organic compounds. Problems such as solvents and harmful by-products are difficult to adapt to the requirements of industrial production. The production of L-ribose by biotransformation by microorganisms or enzymes has become a research hotspot at home and abroad. The synthesis of L-ribose by biotransformation has the characteristics of good stereoselectivity, mild reaction conditions, and less pollution. According to different raw materials, it can be divided into two categories: ribitol as raw material and L-arabinose as raw material. It is worth mentioning that the transformation of L-arabinose into L-ribose requires two steps in recent years. For catalysis, many researchers are committed to using L-arabinose isomerase and mannose-6-phosphate isomerase as an enzyme catalytic system to realize the one-step catalysis of L-arabinose to L-ribose by the two enzymes.

随着基因工程技术的迅速发展,利用分子克隆和外源表达技术可以大幅度地提高某种工业酶在宿主微生物中的表达量,通过这种方法构建的基因工程菌株具有普通微生物难以企及的酶催化效率;利用共表达基因工程菌株生产L-核糖的工艺在国内尚没有报道,本发明选择自筛的发酵乳杆菌和嗜热栖热菌作为分子生物学操作的出发菌株,通过PCR技术从该菌株的基因组上扩增得到了L-阿拉伯糖异构酶的编码基因araA和甘露糖-6-磷酸异构酶的编码基因manA,利用大肠杆菌作为宿主,成功构建了能够高效共表达L-阿拉伯糖异构酶和甘露糖-6-磷酸异构酶的基因工程菌。With the rapid development of genetic engineering technology, molecular cloning and exogenous expression technology can greatly increase the expression of certain industrial enzymes in host microorganisms. The genetically engineered strains constructed by this method have enzymes that are difficult for ordinary microorganisms. Catalytic efficiency; Utilize the technique of co-expression genetic engineering bacterial strain to produce L-ribose at home and do not have report yet, the present invention selects self-screening Lactobacillus fermentum and Thermus thermophilus as the starting strain of molecular biology operation, from this by PCR technology The gene encoding L-arabinose isomerase, araA, and the gene encoding mannose-6-phosphate isomerase, manA, were amplified from the genome of the strain. Using Escherichia coli as the host, a strain capable of efficiently co-expressing L-arabinoisomerase was successfully constructed. Genetically engineered bacteria for sugar isomerase and mannose-6-phosphate isomerase.

发明内容Contents of the invention

本发明所要解决的技术问题是提供一种生产过程简单、条件适宜,能大幅度降低生产成本的基因工程菌。The technical problem to be solved by the present invention is to provide a genetically engineered bacterium with simple production process, suitable conditions and greatly reduced production cost.

本发明还要解决的技术问题是提供上述基因工程菌的构建方法。The technical problem to be solved by the present invention is to provide a method for constructing the above-mentioned genetically engineered bacteria.

本发明最后要解决的技术问题,是提供上述基因工程菌的应用。The final technical problem to be solved by the present invention is to provide the application of the above-mentioned genetically engineered bacteria.

为解决上述技术问题,本发明采用的技术方案如下:In order to solve the problems of the technologies described above, the technical scheme adopted in the present invention is as follows:

一种外源共表达L-阿拉伯糖异构酶和甘露糖-6-磷酸异构酶基因工程菌,其特征在于,其为导入了核苷酸序列SEQ ID NO:1(L-阿拉伯糖异构酶的基因序列,araA)和核苷酸序列SEQ ID NO:2(甘露糖-6-磷酸异构酶的基因序列,manA)的重组大肠杆菌。An exogenous co-expression of L-arabinose isomerase and mannose-6-phosphate isomerase genetically engineered bacteria is characterized in that it is introduced into the nucleotide sequence SEQ ID NO: 1 (L-arabinose isomerase The recombinant Escherichia coli with the gene sequence of mannose-6-phosphate isomerase, araA) and the nucleotide sequence of SEQ ID NO: 2 (the gene sequence of mannose-6-phosphate isomerase, manA).

上述基因工程菌的构建方法,它包括以下步骤:The construction method of above-mentioned genetic engineering bacterium, it comprises the following steps:

(1)含有L-阿拉伯糖异构酶基因和甘露糖-6-磷酸异构酶基因的表达载体的构建:(1) Construction of expression vectors containing L-arabinose isomerase gene and mannose-6-phosphate isomerase gene:

根据Genbank公布的来源于发酵乳杆菌(Lactobacillus fermentum,保藏号:CGMCC2921)和嗜热栖热菌(Thermus thermophilus HB8,ATCC 27634)的L-阿拉伯糖异构酶基因和甘露糖-6-磷酸异构酶基因的序列,运用Vector NTI软件设计下述引物:According to the L-arabinose isomerase gene and mannose-6-phosphate isomerase gene derived from Lactobacillus fermentum (Lactobacillus fermentum, deposit number: CGMCC2921) and Thermus thermophilus HB8 (ATCC 27634) published by Genbank The sequence of enzyme gene, use Vector NTI software to design following primers:

araA-up:5’GGAATTCCATATGCGTAAGATGCAAG3’;araA-up: 5'GGAATTCCATATGCGTAAGATGCAAG3';

araA-down:5’GCGGTACCCTACTTGATGTTGAT3’;araA-down: 5'GCGGTACCCTACTTGATGTTGAT3';

manA-up:5’ATATATCCATGGGTGGGGCCCCGGGTA3’;manA-up: 5'ATATATCCATGGGTGGGGCCCCGGGTA3';

manA-down:5’AGAATTCTCACGCCCCCTCCTT3’;manA-down: 5'AGAATTCTCACGCCCCCCTCCTT3';

分别提取处于对数生长期的发酵乳杆菌基因组DNA和嗜热栖热菌基因组DNA作 为模板,进行PCR扩增,分别得到L-阿拉伯糖异构酶基因和甘露糖-6-磷酸异构酶基因的PCR扩增产物;回收所述L-阿拉伯糖异构酶基因和所述甘露糖-6-磷酸异构酶基因的PCR扩增产物,将L-阿拉伯糖异构酶基因经限制性内切酶Nde I和Kpn I双酶切,与经过同样双酶切的质粒pETDuet-1在T4连接酶的作用下进行连接,得到重组质粒pETDuet-araA;将重组质粒pETDuet-araA转化至感受态大肠杆菌BL21(DE3)中,涂布含有100μg/mL氨苄青霉素的LB固体培养基,37℃培养12~16h得到单克隆;The genomic DNA of Lactobacillus fermentum and Thermus thermophilus in the logarithmic growth phase were extracted respectively as templates, and PCR amplification was performed to obtain the L-arabinose isomerase gene and mannose-6-phosphate isomerase gene respectively PCR amplified product; reclaim the PCR amplified product of described L-arabinose isomerase gene and described mannose-6-phosphate isomerase gene, the L-arabinose isomerase gene is subjected to restriction endonuclease Digest with enzymes Nde I and Kpn I, and connect with the plasmid pETDuet-1 that has undergone the same double digestion under the action of T4 ligase to obtain the recombinant plasmid pETDuet-araA; transform the recombinant plasmid pETDuet-araA into competent Escherichia coli In BL21(DE3), spread LB solid medium containing 100 μg/mL ampicillin and culture at 37°C for 12-16 hours to obtain a single clone;

(2)经抗性培养基筛选得到阳性克隆:(2) Positive clones were obtained by screening with resistant medium:

分别挑取单克隆于5mL含有100μg/mL氨苄青霉素的LB液体培养基中,37℃、200rpm培养过夜,获得L-阿拉伯糖异构酶基因工程菌;Single clones were picked and cultured overnight in 5 mL of LB liquid medium containing 100 μg/mL ampicillin at 37°C and 200 rpm to obtain L-arabinose isomerase genetically engineered bacteria;

(3)对L-阿拉伯糖异构酶基因工程菌进行质粒提取:(3) Carry out plasmid extraction to L-arabinose isomerase genetically engineered bacteria:

对(1)中回收的甘露糖-6-磷酸异构酶基因用限制性内切酶Nco I和EcoR I双酶切,再与经过同样双酶切的质粒pETDuet-araA在T4连接酶的作用下进行连接,得到共表达质粒pETDuet-araA-manA;The mannose-6-phosphate isomerase gene recovered in (1) was double-digested with restriction endonucleases Nco I and EcoR I, and then combined with the same double-digested plasmid pETDuet-araA in the role of T4 ligase The connection was carried out to obtain the co-expression plasmid pETDuet-araA-manA;

(4)将共表达质粒pETDuet-araA-manA转化至宿主细胞中:(4) Transform the co-expression plasmid pETDuet-araA-manA into host cells:

将共表达质粒pETDuet-araA-manA转化至感受态大肠杆菌BL21(DE3)中,涂布含有100μg/mL氨苄青霉素的LB固体培养基,37℃培养12~16h得到单克隆;Transform the co-expression plasmid pETDuet-araA-manA into competent Escherichia coli BL21(DE3), spread LB solid medium containing 100 μg/mL ampicillin, and culture at 37°C for 12-16 hours to obtain a single clone;

(5)经抗性培养基筛选得到阳性克隆:(5) Positive clones were obtained by screening with resistant medium:

分别挑取单克隆于5mL含有100μg/mL氨苄青霉素的LB液体培养基中,37℃、200rpm培养过夜,获得共表达L-阿拉伯糖异构酶和甘露糖-6-磷酸异构酶的基因工程菌。Single clones were picked and cultured overnight in 5 mL LB liquid medium containing 100 μg/mL ampicillin at 37 °C and 200 rpm to obtain genetic engineering that co-expresses L-arabinose isomerase and mannose-6-phosphate isomerase bacteria.

其中,PCR扩增体系为:基因组DNA 2μL,araA-up/manA-up和araA-down/manA-down各2μL,dNTP 4μL,10×Taq缓冲液5μL,Taq酶1μL,ddH2O 34μL;Among them, the PCR amplification system is: genomic DNA 2 μL, araA-up/manA-up and araA-down/manA-down 2 μL each, dNTP 4 μL, 10×Taq buffer 5 μL, Taq enzyme 1 μL, ddH 2 O 34 μL;

PCR反应程序为:94℃预变性2min;94℃变性30s,然后55℃退火30s,72℃延伸2min,循环35次;最后72℃延伸10min。The PCR reaction program was as follows: pre-denaturation at 94°C for 2 min; denaturation at 94°C for 30 s, annealing at 55°C for 30 s, extension at 72°C for 2 min, and 35 cycles; final extension at 72°C for 10 min.

上述的基因工程菌在制备L-核糖中的应用。Application of the above-mentioned genetically engineered bacteria in the preparation of L-ribose.

利用上述基因工程菌,以L-阿拉伯糖为底物制备L-核糖的工艺如下:Utilize above-mentioned genetically engineered bacterium, the process of preparing L-ribose with L-arabinose as substrate is as follows:

(1)基因工程菌的诱导表达:将所述基因工程菌接种于LB液体培养基中培养过夜,然后以0.5~10%(v/v)的接种量转接入LB培养基中,20~40℃发酵培养1~3h,再加入终浓度0.1~10g/L的乳糖或终浓度0.1~1.5mM的异丙基-β-D-硫代吡喃半乳糖苷,并置于20~40℃下诱导表达3~48h,离心收集菌体;(1) Induced expression of genetically engineered bacteria: the genetically engineered bacteria were inoculated in LB liquid medium and cultivated overnight, then transferred into LB medium with an inoculum size of 0.5-10% (v/v), 20-10% (v/v) Ferment at 40°C for 1-3 hours, then add lactose with a final concentration of 0.1-10g/L or isopropyl-β-D-thiogalactopyranoside with a final concentration of 0.1-1.5mM, and place at 20-40°C Induce the expression for 3-48 hours, and collect the bacteria by centrifugation;

或者将所述基因工程菌接种于LB液体培养基中培养过夜,然后以0.5~10%(v/v)的接种量转接入发酵培养基中,直接于20~40℃下诱导表达3~48h,离心收集菌体,其中,所述的发酵培养基包含质量比2∶1∶2的乳糖、蛋白胨或酵母粉和NaCl,pH值为4~10,经高压湿热灭菌处理;Or inoculate the genetically engineered bacterium in LB liquid medium and cultivate overnight, then transfer it into the fermentation medium with an inoculum size of 0.5-10% (v/v), and directly induce the expression of 3-3 48h, centrifuge to collect the bacteria, wherein the fermentation medium contains lactose, peptone or yeast powder and NaCl in a mass ratio of 2:1:2, the pH value is 4-10, and is sterilized by high-pressure moist heat;

(2)转化反应:以25~100g/L L-阿拉伯糖为底物,加入(1)中诱导后的基因工程菌进行转化反应,用量以湿菌计为10~100g/L,pH值为5~12,反应温度40~80℃,转化时间12~48h,反应结束后,液相检测L-核糖的含量;(2) Transformation reaction: use 25-100g/L L-arabinose as the substrate, add the genetically engineered bacteria induced in (1) to carry out the transformation reaction, the dosage is 10-100g/L in terms of wet bacteria, and the pH value is 5~12, the reaction temperature is 40~80°C, the conversion time is 12~48h, after the reaction is completed, the liquid phase detects the content of L-ribose;

或者,以25~100g/L L-阿拉伯糖为底物,加入1~15mmol/L Mn2+离子和0.2~5mmol/L Co2+离子,然后加入(1)中诱导后的基因工程菌进行转化反应,用量以湿菌计为10~100g/L,pH值为5~12,反应温度40~80℃,转化时间12~48h,反应结束后,液相检测L-核糖的含量。Alternatively, use 25-100g/L L-arabinose as a substrate, add 1-15mmol/L Mn 2+ ions and 0.2-5mmol/L Co 2+ ions, and then add the induced genetically engineered bacteria in (1) to carry out For the transformation reaction, the dosage is 10-100g/L in terms of wet bacteria, the pH value is 5-12, the reaction temperature is 40-80°C, and the transformation time is 12-48h. After the reaction, the content of L-ribose is detected by liquid phase.

上述的LB培养基包含质量比2∶1∶2的蛋白胨、酵母粉和NaCl。The above LB medium contains peptone, yeast powder and NaCl in a mass ratio of 2:1:2.

有益效果:本发明的L-阿拉伯糖异构酶和甘露糖-6-磷酸异构酶共表达基因工程菌在适宜条件下可以通过催化L-阿拉伯糖生产L-核糖,一步转化,节约反应时间,转化率高,通过本发明的基因工程菌,L-核糖的转化率达到25~60%,具有良好的产业化前景,低浓度Mn2+和Co2+离子的添加可以大幅度提高酶的酶活力,添加1~15mmol/L Mn2+离子和0.2~5mmol/L Fe2+离子后比不添加金属离子的对照组酶活提高58%。Beneficial effects: the co-expression genetically engineered bacteria of L-arabinose isomerase and mannose-6-phosphate isomerase of the present invention can produce L-ribose by catalyzing L-arabinose under suitable conditions, one-step transformation, saving reaction time , high conversion rate, through the genetically engineered bacteria of the present invention, the conversion rate of L-ribose reaches 25-60%, has good industrialization prospects, and the addition of low-concentration Mn 2+ and Co 2+ ions can greatly improve the activity of the enzyme Enzyme activity, after adding 1-15mmol/L Mn 2+ ions and 0.2-5mmol/L Fe 2+ ions, the enzyme activity of the control group without adding metal ions increased by 58%.

附图说明Description of drawings

图1araA产物PCR的琼脂糖凝胶电泳验证,泳道1~2为araA产物PCR,3为标准DNA分子量,自上而下的条带分别为(kb):15.0,10.0,7.5,5.0,2.5,1.0。Figure 1 agarose gel electrophoresis verification of araA product PCR, lanes 1 to 2 are araA product PCR, 3 is the standard DNA molecular weight, and the bands from top to bottom are (kb): 15.0, 10.0, 7.5, 5.0, 2.5, 1.0.

图2manA产物PCR的琼脂糖凝胶电泳验证,泳道1为标准DNA分子量,自上而下的条带分别为(kb):15.0,10.0,7.5,5.0,2.5,1.0,泳道2~3为manA产物PCR。Figure 2 Agarose gel electrophoresis verification of manA product PCR, lane 1 is the standard DNA molecular weight, the bands from top to bottom are (kb): 15.0, 10.0, 7.5, 5.0, 2.5, 1.0, lanes 2 to 3 are manA Product PCR.

图3重组质粒pETDuet-araA核酸胶验证,其中泳道1~4为重组质粒1~4号对araA的PCR产物,泳道5为标准DNA分子量,自上而下的条带分别为(kb):15.0,10.0,7.5,5.0,2.5,1.0。泳道6为空质粒pETDuet-1的Nde I单切产物,泳道7~10为重组质粒1~4号的NdeI单切产物。Figure 3 Nucleic acid gel verification of the recombinant plasmid pETDuet-araA, in which lanes 1 to 4 are the PCR products of recombinant plasmids 1 to 4 for araA, and lane 5 is the standard DNA molecular weight, and the bands from top to bottom are (kb): 15.0 , 10.0, 7.5, 5.0, 2.5, 1.0. Lane 6 is the NdeI single-cut product of empty plasmid pETDuet-1, and lanes 7-10 are the NdeI single-cut products of recombinant plasmids 1-4.

图4共表达质粒pETDuet-araA-manA的构建示意图。Fig. 4 Schematic diagram of the construction of the co-expression plasmid pETDuet-araA-manA.

图5共表达质粒pETDuet-araA-manA的PCR验证泳道1~6为共表达质粒1~6号对araA的PCR产物,泳道7~12为共表达质粒1~6对manA的PCR产物,泳道13为标准 DNA分子量,自上而下的条带分别为(kb):15.0,10.0,7.5,5.0,2.5,1.0。Figure 5 PCR verification of co-expression plasmid pETDuet-araA-manA Lanes 1-6 are PCR products of co-expression plasmids 1-6 for araA, lanes 7-12 are PCR products of co-expression plasmids 1-6 for manA, and lane 13 It is the standard DNA molecular weight, and the bands from top to bottom are (kb): 15.0, 10.0, 7.5, 5.0, 2.5, 1.0.

图6共表达质粒pETDuet-araA-manA的双酶切验证,泳道1为标准DNA分子量,自上而下的条带分别为(kb):15.0,10.0,7.5,5.0,2.5,1.0。泳道2~3分别为共表达质粒2号的Nde I和Kpn I,Nco I和EcoR I双切产物,泳道4~5分别为共表达质粒3号的Nde I和Kpn I,Nco I和EcoR I双切产物。Figure 6 Double enzyme digestion verification of the co-expression plasmid pETDuet-araA-manA, lane 1 is the standard DNA molecular weight, and the bands from top to bottom are (kb): 15.0, 10.0, 7.5, 5.0, 2.5, 1.0. Swimming lanes 2 to 3 are the double cut products of Nde I and Kpn I, Nco I and EcoR I of co-expression plasmid No. 2, respectively, and lanes 4 to 5 are Nde I, Kpn I, Nco I and EcoR I of co-expression plasmid No. 3, respectively double cut product.

图7L-阿拉伯糖异构酶和甘露糖-6-磷酸异构酶共表达菌株诱导表达SDS-PAGE图,泳道M为标准蛋白分子量,泳道1~2分别为共表达菌株上清和全细胞。Fig. 7 SDS-PAGE diagram of induced expression of L-arabinose isomerase and mannose-6-phosphate isomerase co-expression strains, lane M is standard protein molecular weight, and lanes 1-2 are supernatant and whole cells of co-expression strains respectively.

图8产物混合样的液相检测图谱。The liquid phase detection spectrum of Fig. 8 product mixed sample.

具体实施方式detailed description

根据下述实施例,可以更好地理解本发明。然而,本领域的技术人员容易理解,实施例所描述的内容仅用于说明本发明,而不应当也不会限制权利要求书中所详细描述的本发明。The present invention can be better understood from the following examples. However, those skilled in the art can easily understand that the content described in the embodiments is only for illustrating the present invention, and should not and will not limit the present invention described in the claims.

实施例1:含有L-阿拉伯糖异构酶基因和甘露糖-6-磷酸异构酶基因的共表达质粒载体的构建。Example 1: Construction of a co-expression plasmid vector containing L-arabinose isomerase gene and mannose-6-phosphate isomerase gene.

根据Genbank上已报道的来源于发酵乳杆菌(Lactobacillus fermentum,保藏号:CGMCC2921)和嗜热栖热菌(Thermus thermophilus HB8,ATCC 27634)的L-阿拉伯糖异构酶基因和甘露糖-6-磷酸异构酶基因的序列,运用Vector NTI软件设计引物,引物序列如表1所示:According to the L-arabinose isomerase gene and mannose-6-phosphate derived from Lactobacillus fermentum (Lactobacillus fermentum, deposit number: CGMCC2921) and Thermus thermophilus HB8 (ATCC 27634) reported on Genbank The sequence of the isomerase gene uses Vector NTI software to design primers, and the primer sequences are as shown in Table 1:

表1引物序列Table 1 Primer Sequence

按照生产商提供的使用说明书,用Genomic DNA Purification Kit(Takara,大连) 抽提处于对数生长期的发酵乳杆菌NXTag1(Lactobacillus fermentum,保藏号:CGMCC2921,其公开于专利文献ZL200910025982.9)和嗜热栖热菌(Thermus thermophilus,HB8,ATCC 27634)的基因组DNA,并用1%(10g/L)琼脂糖凝胶电泳对所获得的基因组DNA进行检测,分别以提取的发酵乳杆菌基因组DNA和嗜热栖热菌基因组DNA作为模板,进行PCR扩增。According to the instructions provided by the manufacturer, the Genomic DNA Purification Kit (Takara, Dalian) was used to extract Lactobacillus fermentum NXTag1 (Lactobacillus fermentum, deposit number: CGMCC2921, which was disclosed in the patent document ZL200910025982. Genomic DNA of Thermus thermophilus (Thermus thermophilus, HB8, ATCC 27634), and the obtained genomic DNA was detected by 1% (10g/L) agarose gel electrophoresis, and the extracted Lactobacillus fermentum genomic DNA and Genomic DNA of Thermus thermica was used as a template for PCR amplification.

PCR(聚合酶链式反应)的扩增体系为:基因组DNA2pL,引物araA-up(manA-up)和引物araA-down(manAdown)各2μL,dNTP 4μL,10×Taq缓冲液5μL,Taq酶1μL,ddH2O 34μL;The amplification system of PCR (polymerase chain reaction) is: genomic DNA 2pL, primer araA-up (manA-up) and primer araA-down (manAdown) 2 μL each, dNTP 4 μL, 10×Taq buffer 5 μL, Taq enzyme 1 μL , ddH 2 O 34 μL;

PCR反应程序为:94℃预变性2min;94℃变性30s,然后55℃退火30s,72℃延伸2min,循环35次;最后72℃延伸10min;The PCR reaction program was: pre-denaturation at 94°C for 2 minutes; denaturation at 94°C for 30 seconds, then annealing at 55°C for 30 seconds, extension at 72°C for 2 minutes, and 35 cycles; finally, extension at 72°C for 10 minutes;

将PCR产物于1%(10g/L)琼脂糖凝胶电泳验证,结果见图1和图2。发现分别与预期分子量(1424bp和900bp)大小相符的DNA条带后分别用Axygen公司的柱式割胶回收试剂盒回收。The PCR product was verified by 1% (10 g/L) agarose gel electrophoresis, and the results are shown in Fig. 1 and Fig. 2 . After DNA bands corresponding to the expected molecular weight (1424bp and 900bp) were found, they were recovered with the Axygen company's column type rubber tapping recovery kit.

用预先设计在引物序列中酶切位点所对应的限制性内切酶对(2)中获得的PCR产物araA进行酶切反应。所用的限制性内切酶是EcoRI和Hind III。酶切体系为:PCR产物12.5μL,Nde I 1μL,Kpn I 1μL,10×M缓冲液2.5μL,ddH2O 8μL,总体积25μL。将酶切后的PCR产物经过DNA纯化试剂盒纯化。The PCR product araA obtained in (2) was digested with the restriction endonuclease corresponding to the restriction site in the primer sequence designed in advance. The restriction enzymes used were EcoRI and Hind III. The digestion system is: 12.5 μL of PCR product, 1 μL of Nde I, 1 μL of Kpn I, 2.5 μL of 10×M buffer, 8 μL of ddH 2 O, and a total volume of 25 μL. The digested PCR product was purified by a DNA purification kit.

使用同样的限制性内切酶和酶切体系对pETDuet-1质粒进行酶切,由于所选用的两个酶切位点在pETDuet-1质粒的多克隆位点(Multiple Cloning Site,MCS)上相距很近(约20bp),因此酶切之后的质粒只需要经过DNA纯化试剂盒即可达到纯化的目的。The pETDuet-1 plasmid was digested with the same restriction endonuclease and restriction enzyme system, because the two selected restriction sites were separated from each other on the multiple cloning site (Multiple Cloning Site, MCS) of the pETDuet-1 plasmid It is very close (about 20bp), so the digested plasmid only needs to pass through the DNA purification kit to achieve the purpose of purification.

将经过纯化的PCR产物和pETDuet-1质粒进行连接。连接反应体系为:酶切纯化的PCR产物6μL,酶切纯化的pETDuet-1质粒2μL,T4连接酶1μL,10×T4连接酶缓冲液1μL。在37℃连接2h后即可获得重组质粒pETDuet-araA。The purified PCR product was ligated with pETDuet-1 plasmid. The ligation reaction system was: 6 μL of digested and purified PCR product, 2 μL of digested and purified pETDuet-1 plasmid, 1 μL of T4 ligase, and 1 μL of 10×T4 ligase buffer. The recombinant plasmid pETDuet-araA can be obtained after ligation at 37°C for 2 hours.

重组质粒pETDuet-araA转化感受态大肠杆菌细胞使用氯化钙法:The recombinant plasmid pETDuet-araA is used to transform competent E. coli cells using the calcium chloride method:

(1)取10μL重组质粒pETDuet-araA于50μL大肠杆菌Escherichia coli BL21(DE3)感受态细胞中,冰浴30min。(1) Take 10 μL of the recombinant plasmid pETDuet-araA in 50 μL of Escherichia coli BL21 (DE3) competent cells, and place in ice bath for 30 minutes.

(2)42℃水浴热激90s,快速置于冰上2~3min。(2) Heat shock in a water bath at 42°C for 90 seconds, and quickly place on ice for 2-3 minutes.

(3)加入新鲜LB液体培养基800μL,于37℃振荡培养45min。(3) Add 800 μL of fresh LB liquid medium, shake and culture at 37° C. for 45 minutes.

(4)取200μL菌体涂布于含有100μg/mL氨苄青霉素的LB固体培养基表面。37℃ 培养12~16h至单菌落出现。(4) Take 200 μL of bacteria and spread on the surface of LB solid medium containing 100 μg/mL ampicillin. Cultivate at 37°C for 12-16 hours until a single colony appears.

重组子pETDuet-araA的鉴定:将单菌落接种于含有氨苄青霉素(100μg/mL)的LB液体培养基中37℃过夜培养并分别提取质粒,对各质粒进行菌落PCR验证,再按照“限制性酶切反应,纯化及连接反应”中的酶切体系和条件用Nde I对空质粒pETDuet-1和重组质粒pETDuet-araA分别进行单酶切,将菌落PCR产物和酶切产物进行琼脂糖凝胶电泳鉴定,结果如图3所示。实验结果说明获得的重组质粒pETDuet-araA是正确的。Identification of the recombinant pETDuet-araA: inoculate a single colony in LB liquid medium containing ampicillin (100 μg/mL) and culture overnight at 37°C and extract the plasmids respectively, perform colony PCR verification on each plasmid, and then follow the "restriction enzyme Digestion system and conditions in "Digestion Reaction, Purification and Ligation Reaction" Use Nde I to perform single enzyme digestion on the empty plasmid pETDuet-1 and recombinant plasmid pETDuet-araA respectively, and perform agarose gel electrophoresis on the colony PCR product and the digested product Identification, the results are shown in Figure 3. The experimental results show that the obtained recombinant plasmid pETDuet-araA is correct.

经电泳结果证实,该阳性克隆菌落含有DNA片段插入质粒pETDuet-araA,含此重组质粒pETDuet-araA的重组大肠杆菌即为转化的重组大肠杆菌BL21-araA。测序结果显示插入片段含有一个长1424bp的开放阅读框架(Open Reading Frame,ORF)。manA基因的限制性酶切反应,纯化及连接反应:用预先设计在引物序列中酶切位点所对应的限制性内切酶对获得的PCR产物manA和重组质粒pETDuet-araA进行酶切反应。所用的限制性内切酶是Nco I和EcoR I。酶切体系为:PCR产物12.5μL,Nco I 1μL,EcoR I 1μL,10×M缓冲液2.5μL,ddH2O8μL,总体积25μL。将酶切后的PCR产物和重组质粒经过DNA纯化试剂盒纯化。The results of electrophoresis confirmed that the positive cloned colony contained a DNA fragment inserted into the plasmid pETDuet-araA, and the recombinant Escherichia coli containing the recombinant plasmid pETDuet-araA was the transformed recombinant Escherichia coli BL21-araA. Sequencing results showed that the insert contained a 1424bp open reading frame (Open Reading Frame, ORF). Restriction enzyme digestion reaction, purification and ligation reaction of manA gene: Use the restriction endonuclease corresponding to the restriction endonuclease in the primer sequence designed in advance to carry out enzyme digestion reaction on the obtained PCR product manA and recombinant plasmid pETDuet-araA. The restriction enzymes used were Nco I and EcoR I. The digestion system is: 12.5 μL of PCR product, 1 μL of Nco I, 1 μL of EcoR I, 2.5 μL of 10×M buffer, 8 μL of ddH 2 O, and a total volume of 25 μL. The digested PCR products and recombinant plasmids were purified by a DNA purification kit.

将经过纯化的PCR产物和pETDuet-araA重组质粒进行连接。连接反应体系为:酶切纯化的PCR产物5μL,酶切纯化的pETDuet-araA质粒3μL,T4连接酶1μL,10×T4连接酶缓冲液1μL。在37℃连接2h后即可获得共表达质粒pETDuet-araA-manA,其主要结构如图4所示。The purified PCR product was ligated with the pETDuet-araA recombinant plasmid. The ligation reaction system was: 5 μL of digested and purified PCR product, 3 μL of digested and purified pETDuet-araA plasmid, 1 μL of T4 ligase, and 1 μL of 10×T4 ligase buffer. The co-expression plasmid pETDuet-araA-manA can be obtained after ligation at 37°C for 2 hours, and its main structure is shown in Figure 4.

共表达质粒pETDuet-araA-manA转化感受态大肠杆菌细胞使用氯化钙法,方法同上述重组质粒pETDuet-araA转化感受态大肠杆菌细胞使用的氯化钙法。The co-expression plasmid pETDuet-araA-manA was used to transform competent E. coli cells using the calcium chloride method, which was the same as the calcium chloride method used to transform competent E. coli cells with the above-mentioned recombinant plasmid pETDuet-araA.

重组子pETDuet-araA-lacZ的鉴定:将单菌落接种于含有氨苄青霉素(100μg/mL)的LB液体培养基中37℃过夜培养并分别提取质粒,对各质粒进行菌落PCR验证,再按照上述的限制性酶切、纯化及连接反应中的酶切体系和条件分别用Nde I和KpnI,NcoI和EcoRI对共表达质粒pETDuet-araA-manA进行双酶切,将菌落PCR产物和双酶切产物进行琼脂糖凝胶电泳鉴定。鉴定结果见图5和图6,实验结果说明获得的共表达质粒pETDuet-araA-manA 3号是正确的。Identification of the recombinant pETDuet-araA-lacZ: Inoculate a single colony in LB liquid medium containing ampicillin (100 μg/mL) and culture overnight at 37°C and extract the plasmids respectively, perform colony PCR verification on each plasmid, and then follow the above-mentioned Enzyme digestion system and conditions in restriction enzyme digestion, purification and ligation reactions Use Nde I and KpnI, NcoI and EcoRI to perform double enzyme digestion on the co-expression plasmid pETDuet-araA-manA, respectively, and carry out the colony PCR product and the double enzyme digestion product Identification by agarose gel electrophoresis. The identification results are shown in Figure 5 and Figure 6, and the experimental results show that the obtained co-expression plasmid pETDuet-araA-manA No. 3 is correct.

经电泳结果证实,如图5和图6所示,该阳性克隆菌落含有DNA片段插入质粒pETDuet-araA-manA,含此共表达质粒pETDuet-araA-manA的重组大肠杆菌即为转化的重组大肠杆菌BL21-araA-manA。测序结果显示插入片段含有一个长1424bp的开放阅读 框架(Open Reading Frame,ORF)和一个长900bp的开放阅读框架。It was confirmed by electrophoresis results, as shown in Figure 5 and Figure 6, that the positive cloned colony contained a DNA fragment inserted into the plasmid pETDuet-araA-manA, and the recombinant Escherichia coli containing this co-expression plasmid pETDuet-araA-manA was the transformed recombinant Escherichia coli BL21-araA-manA. Sequencing results showed that the insert contained a 1424bp open reading frame (Open Reading Frame, ORF) and a 900bp open reading frame.

实施例2:基因工程菌的诱导表达。Example 2: Induced expression of genetically engineered bacteria.

采用两种方式对实施例1中获得的基因工程菌诱导表达:Two ways are used to induce expression of the genetically engineered bacteria obtained in Example 1:

(1)配制种子液1L,培养基为LB液体培养基(蛋白胨10g/L、酵母粉5g/L、NaCl 10g/L,经121℃高压湿热灭菌30min后装入数个500mL广口三角瓶中。用接种针向种子液接入一环实施例1中基因工程菌菌种,并置于37℃摇床以200rpm的转速过夜培养。配制含有蛋白胨10g/L、酵母粉5g/L、NaCl 10g/L的LB培养基1000mL,分装于容量500mL的广口三角瓶中,每瓶的装液量为100mL;将上述LB培养基于121℃高压湿热灭菌30min。待培养基冷却后接入过夜培养的种子液1mL,将三角瓶置于37℃摇床以200rpm的转速培养,约1.5h后加入终浓度为0.1~10g/L的乳糖或者终浓度为1mM的IPTG(异丙基-β-D-硫代吡喃半乳糖苷),并置于37℃摇床以200rpm转速进行诱导作用6h,得到共表达基因工程菌发酵液A,发酵液离心收集得到共表达基因工程菌菌体A。(1) Prepare 1 L of seed solution, the medium is LB liquid medium (peptone 10g/L, yeast powder 5g/L, NaCl 10g/L, sterilized by high pressure at 121°C for 30min, and then put it into several 500mL wide-mouthed triangular flasks In. Use an inoculation needle to insert a ring of genetically engineered bacterial strains in Example 1 into the seed solution, and place it on a shaker at 37° C. to cultivate overnight at a speed of 200 rpm. The preparation contains 10 g/L of peptone, 5 g/L of yeast powder, and NaCl 1000mL of 10g/L LB culture medium was divided into wide-mouthed Erlenmeyer flasks with a capacity of 500mL. 1mL of the seed solution cultivated overnight, put the Erlenmeyer flask on a shaker at 37°C and cultivate it at a speed of 200rpm. After about 1.5h, add lactose with a final concentration of 0.1-10g/L or IPTG with a final concentration of 1mM (isopropyl-β -D-thiogalactopyranoside), and placed in a shaker at 37° C. for 6 hours at a speed of 200 rpm to obtain a co-expressed genetically engineered bacterium fermentation broth A, and the fermentation broth was collected by centrifugation to obtain a co-expressed genetically engineered bacterium cell A .

(2)配制种子液l L,培养基为LB液体培养基(蛋白胨10g/L、酵母粉5g/L、NaCl10g/L,用NaOH调节pH值为7.0),经121℃高压湿热灭菌30min后装入数个500mL广口三角瓶中。用接种针向种子液接入一环基因工程菌菌种,并置于37℃摇床以200rpm的转速过夜培养。配制含有乳糖10g/L、蛋白胨(或酵母粉)5g/L、氯化钠10g/L的发酵培养基1000mL,分装于容量500mL的广口三角瓶中,每瓶的装液量为100mL;将上述发酵培养基于121℃高压湿热灭菌30min。待培养基冷却后接入过夜培养的种子液1mL,将三角瓶置于25℃摇床以200rpm的转速培养,乳糖既作碳源又作为诱导剂,进行诱导作用22h,得到共表达基因工程菌发酵液B。发酵液离心收集,得到共表达基因工程菌菌体B,通过SDS-PAGE检测,结果如图7所示。(2) Prepare 1 L of seed solution, the medium is LB liquid medium (peptone 10g/L, yeast powder 5g/L, NaCl 10g/L, adjust the pH value to 7.0 with NaOH), after sterilizing by high pressure at 121°C for 30min Put it into several 500mL wide-mouth Erlenmeyer flasks. Inject a ring of genetically engineered strains into the seed solution with an inoculation needle, and place it on a shaker at 37°C at a speed of 200rpm for overnight cultivation. Prepare 1000 mL of fermentation medium containing 10 g/L of lactose, 5 g/L of peptone (or yeast powder), and 10 g/L of sodium chloride, and distribute it in a wide-mouthed conical flask with a capacity of 500 mL. The liquid volume of each bottle is 100 mL; The above fermentation culture was sterilized based on 121° C. high-pressure damp heat for 30 minutes. After cooling the culture medium, insert 1mL of the overnight cultured seed solution, place the flask in a shaker at 25°C and cultivate it at a speed of 200rpm, use lactose as both a carbon source and an inducer, and induce for 22 hours to obtain co-expressed genetically engineered bacteria Fermentation Broth B. The fermentation broth was collected by centrifugation to obtain co-expressed genetically engineered bacterial cell B, which was detected by SDS-PAGE, and the results are shown in FIG. 7 .

实施例3:金属离子种类及浓度对共表达L-阿拉伯糖异构酶和甘露糖-6-磷酸异构酶基因工程菌株酶活的影响。Example 3: Effects of the type and concentration of metal ions on the enzyme activity of a genetically engineered strain co-expressing L-arabinose isomerase and mannose-6-phosphate isomerase.

向1mL 100mM磷酸钠缓冲溶液(pH 6.5)中添加L-阿拉伯糖至终浓度为100mM,再加入共表达基因工程菌菌体12mg,各金属离子的添加终浓度为1mM或者10mM,65℃水浴20min,通过HPLC测定生成的L-核糖的生成量,测定结果如表2所示(以未添加 金属离子组为对照,设定酶活为100%)。Add L-arabinose to 1 mL of 100 mM sodium phosphate buffer solution (pH 6.5) to a final concentration of 100 mM, then add 12 mg of co-expressed genetically engineered bacteria, and add the final concentration of each metal ion to 1 mM or 10 mM, and bathe in water at 65 ° C for 20 min , the generation amount of the L-ribose that generates by HPLC measurement, measurement result is as shown in table 2 (with no metal ion group as contrast, enzymatic activity is set as 100%).

表2不同金属离子及浓度对共表达基因工程菌株酶活力的影响Table 2 Effects of different metal ions and concentrations on the enzyme activity of co-expressed genetically engineered strains

从结果中可以看出,当Co2+浓度为1mM、Mn2+浓度为10mM时酶活较高,固在用共表达基因工程菌制备L-核糖时添加离子浓度为Co2+1mM、Mn2+10mM。As can be seen from the results, when the Co 2+ concentration is 1mM and the Mn 2+ concentration is 10mM, the enzyme activity is higher, and the added ion concentration is Co 2+ 1mM, Mn 2+ 10mM.

实施例4:利用共表达基因工程菌制备L-核糖(不加金属离子)。Example 4: Preparation of L-ribose (without adding metal ions) by co-expressing genetically engineered bacteria.

取1.2g离心收集的共表达基因工程菌菌体A投入到100mM pH6.5磷酸钠缓冲配置的30g/L L-阿拉伯糖进行催化反应,反应条件是温度65℃,摇床转速180rpm。每4小时取样,测定生成的L-核糖含量,29h后反应结束。HPLC检测L-核糖的转化率达到17%。Take 1.2g of the co-expressed genetically engineered bacterial cell A collected by centrifugation and put it into 30g/L L-arabinose buffered with 100mM pH6.5 sodium phosphate buffer for catalytic reaction. The reaction conditions are temperature 65°C and shaker speed 180rpm. Samples were taken every 4 hours to measure the generated L-ribose content, and the reaction ended after 29 hours. The conversion rate of L-ribose was detected by HPLC to reach 17%.

实施例5:利用共表达基因工程菌制备L-核糖(加金属离子)。Example 5: Preparation of L-ribose (adding metal ions) by co-expressing genetically engineered bacteria.

取1.2g离心收集的共表达基因工程菌菌体B,将收集的菌体投入100mM pH6.5磷酸钠缓冲配置的30g/L L-阿拉伯糖进行催化反应,反应条件是温度50℃,添加10mM Mn2+和1mM Co2+,摇床转速180rpm。每4小时取样,测定生成的L-核糖含量,29h后反应结束。经HPLC检测L-核糖的转化率达到32%。Take 1.2g of the co-expressed genetically engineered bacterial cell B collected by centrifugation, put the collected cell into 30g/L L-arabinose buffered with 100mM pH6.5 sodium phosphate buffer for catalytic reaction, the reaction conditions are temperature 50°C, add 10mM Mn 2+ and 1mM Co 2+ , the shaker rotates at 180rpm. Samples were taken every 4 hours to measure the generated L-ribose content, and the reaction ended after 29 hours. The conversion rate of L-ribose was detected by HPLC to reach 32%.

实施例6:Embodiment 6:

利用共表达基因工程菌制备L-核糖,方法同实施例5,不同的是,共表达基因工程菌菌体B用量为3.6g,底物L-阿拉伯糖的浓度为60g/L,反应温度为65℃,反应时间为24h。经HPLC检测L-核糖的转化率达到43%,如图8所示。Utilize the co-expression genetically engineered bacteria to prepare L-ribose, the method is the same as in Example 5, the difference is that the amount of co-expressed genetically engineered bacteria thalline B is 3.6g, the concentration of the substrate L-arabinose is 60g/L, and the reaction temperature is 65°C, the reaction time is 24h. The conversion rate of L-ribose was detected by HPLC to reach 43%, as shown in FIG. 8 .

实施例7:Embodiment 7:

利用共表达基因工程菌制备L-核糖,方法同实施例5,不同的是,取3.6g离心收集的共表达基因工程菌菌体A,底物L-阿拉伯糖的浓度为100g/L。经HPLC检测L-核糖的转化率达到28%。L-ribose was prepared by co-expressing genetically engineered bacteria, the method was the same as in Example 5, except that 3.6 g of co-expressing genetically engineered bacteria cell A collected by centrifugation was used, and the concentration of the substrate L-arabinose was 100 g/L. The conversion rate of L-ribose was detected by HPLC to reach 28%.

实施例8:Embodiment 8:

利用共表达基因工程菌制备L-核糖,方法同实施例5,不同的是,反应温度为65℃,反应时间为25h。经HPLC检测L-核糖的转化率达到36%。The method for preparing L-ribose by co-expressing genetically engineered bacteria is the same as in Example 5, except that the reaction temperature is 65° C. and the reaction time is 25 hours. The conversion rate of L-ribose was detected by HPLC to reach 36%.

实施例9:利用共表达基因工程菌制备L-核糖,方法同实施例5,不同的是,底物L-阿拉伯糖的浓度为100g/L,反应时间为36h。经HPLC检测L-核糖的转化率达到18%。Example 9: Preparation of L-ribose by co-expressing genetically engineered bacteria, the method is the same as in Example 5, except that the concentration of the substrate L-arabinose is 100 g/L, and the reaction time is 36 hours. The conversion rate of L-ribose was detected by HPLC to reach 18%.

实施例10:Example 10:

利用共表达基因工程菌制备L-核糖,方法同实施例5,不同的是,所用的菌体为共表达基因工程菌体A,反应时间为30h,HPLC检测L-核糖的转化率达到21%。Utilize co-expression genetically engineered bacteria to prepare L-ribose, the method is the same as in Example 5, the difference is that the thalline used is co-expressed genetically engineered bacterium A, the reaction time is 30h, and the conversion rate of L-ribose detected by HPLC reaches 21%. .

实施例11:Example 11:

利用共表达基因工程菌制备L-核糖,方法同实施例5,不同的是,所用的菌体为共表达基因工程菌体A,菌体量为3.6g,反应时间为28h,HPLC检测L-核糖的转化率达到25%。Utilize co-expression genetically engineered bacteria to prepare L-ribose, the method is the same as in Example 5, the difference is that the thalline used is co-expression genetically engineered thalline A, the thalline amount is 3.6g, and the reaction time is 28h, HPLC detects L-ribose The conversion rate of ribose reaches 25%.

Claims (5)

1. coexpression L-arabinose isomerase gene and a genetic engineering bacterium for mannose-6-phosphate isomerase, its feature Being, it is to have imported nucleotide sequence SEQ ID NO:1 and the recombination bacillus coli of nucleotide sequence SEQ ID NO:2, its In, described SEQ ID NO:1 derives from lactobacillus fermenti, and SEQ ID NO:2 derives from thermus thermophilus, described genetic engineering The construction method of bacterium comprises the steps:
(1)
The L-arabinose isomerase gene deriving from lactobacillus fermenti and thermus thermophilus announced according to Genbank and sweet dew The sequence of sugar-6-phosphate isomerases gene, utilization Vector NTI Software for Design following primer:
AraA-up:5 ' GGAATTCCATATGCGTAAGATGCAAG3 ';
AraA-down:5 ' GCGGTACCCTACTTGATGTTGAT3 ';
ManA-up:5 ' ATATATCCATGGGTGGGGCCCCGGGTA3 ';
ManA-down:5 ' AGAATTCTCACGCCCCCTCCTT3 ';
Extract respectively and be in the lactobacillus fermenti genomic DNA of exponential phase and thermus thermophilus genomic DNA as template, Carrying out PCR amplification, the PCR amplification respectively obtaining L-arabinose isomerase gene and mannose-6-phosphate isomerase gene is produced Thing;Reclaim described L-arabinose isomerase gene and the pcr amplification product of described mannose-6-phosphate isomerase gene, will L-arabinose isomerase gene through restriction enzyme Nde I and Kpn I double digestion, with through as the plasmid of double digestion PETDuet-1 is attached under the effect of T4 ligase, obtains recombinant plasmid pETDuet-araA;By recombinant plasmid PETDuet-araA converts to competence e. coli bl21 (DE3), then coats containing 100 μ g/mL ampicillins LB solid medium, cultivate for 37 DEG C and 12~16h obtain monoclonal;
(2) positive colony is obtained through the screening of resistance culture base:
Picking monoclonal is in 5mL contains the LB fluid nutrient medium of 100 μ g/mL ampicillins respectively, 37 DEG C, 200rpm cultivation Overnight, it is thus achieved that L-arabinose isomerase genetic engineering bacterium;
(3) L-arabinose isomerase genetic engineering bacterium is carried out plasmid extraction, different to the Man-6-P reclaimed in (1) Structure enzyme gene restriction enzyme Nco I and EcoR I double digestion, then with through as the plasmid pETDuet-of double digestion AraA is attached under the effect of T4 ligase, obtains co-expression plasmid pETDuet-araA-manA;
(4) co-expression plasmid pETDuet-araA-manA is converted to host cell:
Co-expression plasmid pETDuet-araA-manA is converted in competence e. coli bl21 (DE3), coat containing The LB solid medium of 100 μ g/mL ampicillins, cultivates 12~16h for 37 DEG C and obtains monoclonal;
(5) positive colony is obtained through the screening of resistance culture base:
Picking monoclonal is in 5mL contains the LB fluid nutrient medium of 100 μ g/mL ampicillins respectively, 37 DEG C, 200rpm cultivation Overnight, it is thus achieved that coexpression L-arabinose isomerase and the genetic engineering bacterium of mannose-6-phosphate isomerase.
Genetic engineering bacterium the most according to claim 1, it is characterised in that wherein PCR amplification system is: genomic DNA 2 μ The each 2 μ L of L, araA-up/manA-up and araA-down/manA-down, dNTP 4 μ L, 10 × Taq buffer solution 5 μ L, Taq enzyme 1 μ L, ddH2O 34μL;
PCR response procedures is: 94 DEG C of denaturations 2min;94 DEG C of sex change 30s, then 55 DEG C of annealing 30s, 72 DEG C extend 2min, follow Ring 35 times;Last 72 DEG C extend 10min.
3. the application in preparing L-ribose of the genetic engineering bacterium described in claim 1.
Application the most according to claim 3, it is characterised in that utilize genetic engineering bacterium, with Arabinose for substrate system The technique of standby L-ribose is as follows:
(1) abduction delivering of genetic engineering bacterium: described genetic engineering bacterium is inoculated in overnight incubation in LB fluid nutrient medium, then Transfer in LB culture medium with the inoculum concentration of 0.5~10% (v/v), 20~40 DEG C of fermented and cultured 1~3h, add final concentration eventually The lactose of concentration 0.1~10g/L or the isopropyl-beta D-thio galactopyranoside of 0.1~1.5mM, be placed in 20~40 Abduction delivering 3~48h at DEG C, centrifugal collection thalline;
Or described genetic engineering bacterium is inoculated in overnight incubation in LB fluid nutrient medium, then with 0.5~the connecing of 10% (v/v) The amount of kind is transferred in fermentation medium, abduction delivering 3~48h at 20~40 DEG C, centrifugal thalline of collecting, and wherein, described sends out Ferment culture medium comprises the lactose of mass ratio 2: 1: 2, peptone or dusty yeast and NaCl, and pH value is 4~10, through high pressure moist heat sterilization Process;
(2) conversion reaction: with 25~100g/L Arabinoses as substrate, adds the genetic engineering bacterium after inducing in (1) and carries out Conversion reaction, consumption is calculated as 10~100g/L with wet bacterium, and pH value is 5~12, reaction temperature 40~80 DEG C, transformation time 12~ 48h, after reaction terminates, the content of liquid phase detection L-ribose;
Or, with 25~100g/L Arabinoses as substrate, add 1~15mmol/L Mn2+Ion and 0.2~5mmol/L Co2+Ion, is subsequently adding the genetic engineering bacterium after inducing in (1) and carries out conversion reaction, and consumption is calculated as 10~100g/L with wet bacterium, PH value is 5~12, reaction temperature 40~80 DEG C, transformation time 12~48h, after reaction terminates, and the content of liquid phase detection L-ribose.
Application the most according to claim 4, it is characterised in that it is 2 that the LB culture medium described in step (1) comprises mass ratio : peptone, dusty yeast and the NaCl of 1: 2.
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