CN103060217B - Recombinant yeast strain capable of efficiently metabolizing xylose and application thereof - Google Patents
Recombinant yeast strain capable of efficiently metabolizing xylose and application thereof Download PDFInfo
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Abstract
Description
技术领域technical field
本发明属于生物工程技术领域,具体涉及一株能够发酵木糖产乙醇的重组酵母菌株。The invention belongs to the technical field of bioengineering, in particular to a recombinant yeast strain capable of fermenting xylose to produce ethanol.
背景技术Background technique
利用木质纤维素生产燃料乙醇,不仅能够降低燃料乙醇的生产成本,而且在改善环境及废物处理等方面均有很重要的作用。我国作为一个农业大国,秸秆等农作物废弃物资源相当丰富,这为发展燃料乙醇产业提供了得天独厚的条件。一般用作工业生产乙醇的菌株为酿酒酵母,虽然天然的酿酒酵母能够很好的利用木质纤维素水解物中的己糖产生乙醇,但是却缺乏对含量丰富的戊糖,例如木糖的代谢能力。因此构建能够高效利用木糖的工程菌株对降低燃料乙醇的生产成本具有关键意义。Utilizing lignocellulose to produce fuel ethanol can not only reduce the production cost of fuel ethanol, but also play an important role in improving the environment and waste disposal. As a large agricultural country, our country is rich in crop waste resources such as straw, which provides unique conditions for the development of fuel ethanol industry. Saccharomyces cerevisiae is generally used for industrial production of ethanol. Although natural Saccharomyces cerevisiae can use the hexose sugar in lignocellulose hydrolyzate to produce ethanol, it lacks the ability to metabolize abundant pentose sugars, such as xylose. . Therefore, the construction of engineering strains that can efficiently utilize xylose is of key significance for reducing the production cost of fuel ethanol.
目前我国在利用代谢工程方法构建能够利用木糖产生乙醇的酿酒酵母工程菌株方面已经取得了一定的进展,但是仍不能满足生产的要求,主要表现在木糖利用缓慢、副产物木糖醇积累过多以及乙醇得率低等方面。At present, my country has made some progress in the construction of Saccharomyces cerevisiae engineering strains that can use xylose to produce ethanol using metabolic engineering methods, but it still cannot meet the production requirements, mainly due to the slow utilization of xylose and excessive accumulation of by-product xylitol. Many and low ethanol yield.
发明内容Contents of the invention
本发明的目的是克服现有技术的不足,提供一株高效代谢木糖的重组酵母菌株。The purpose of the present invention is to overcome the deficiencies of the prior art and provide a recombinant yeast strain that metabolizes xylose efficiently.
本发明的第二个目的是提供上述一株高效代谢木糖的重组酵母菌株的用途。The second object of the present invention is to provide the use of the above-mentioned recombinant yeast strain that efficiently metabolizes xylose.
本发明的技术方案概述如下:Technical scheme of the present invention is summarized as follows:
一株高效代谢木糖的重组酵母菌株,分类命名:酿酒酵母(Saccharomyces cerevisiae)命名为SyBE005,已保藏于中国微生物菌种保藏管理委员会普通微生物中心,保藏编号为CGMCC No.6634,其具有高效代谢木糖产乙醇的能力。A recombinant yeast strain that efficiently metabolizes xylose, classified and named: Saccharomyces cerevisiae named SyBE005, has been preserved in the General Microbiology Center of China Committee for the Collection of Microbial Cultures, and the preservation number is CGMCC No.6634, which has high-efficiency metabolism The ability of xylose to produce ethanol.
上述菌株代谢木糖产乙醇的用途。The use of the above bacterial strains to metabolize xylose to produce ethanol.
本发明的优点:Advantages of the present invention:
本发明的重组酵母菌株SyBE005能够有效的利用木糖发酵产生乙醇。乙醇产率达到理论得率的64%,副产物木糖醇的产率在12%以下,能够高效地转化木糖为乙醇,是优良的利用纤维素水解液的菌株。The recombinant yeast strain SyBE005 of the present invention can effectively utilize xylose to ferment and produce ethanol. The yield of ethanol reaches 64% of the theoretical yield, and the yield of by-product xylitol is below 12%. It can efficiently convert xylose into ethanol, and is an excellent strain for utilizing cellulose hydrolyzate.
本发明的高效代谢木糖的重组酵母菌株(Saccharomyces cerevisiae)命名为SyBE005,已于2012年9月27日保藏于中国微生物菌种保藏管理委员会普通微生物中心,简称CGMCC,保藏编号为CGMCC No.6634。地址在北京市朝阳区大屯路,中国科学院微生物研究所。The recombinant yeast strain (Saccharomyces cerevisiae) that efficiently metabolizes xylose of the present invention is named SyBE005, and it has been preserved in the General Microbiology Center of the China Committee for Microbial Culture Collection on September 27, 2012, referred to as CGMCC, and the preservation number is CGMCC No.6634 . The address is Datun Road, Chaoyang District, Beijing, Institute of Microbiology, Chinese Academy of Sciences.
附图说明Description of drawings
图1为含有木糖还原酶基因编码框、木糖醇脱氢酶基因编码框及木酮糖激酶基因编码框的质粒图谱。Fig. 1 is a plasmid map containing a xylose reductase gene coding frame, a xylitol dehydrogenase gene coding frame and a xylulokinase gene coding frame.
图2为含有木糖醇脱氢酶基因编码框的质粒pRS305-XDH图谱。Fig. 2 is a map of the plasmid pRS305-XDH containing the coding frame of the xylitol dehydrogenase gene.
图3是含有核糖磷酸异构酶基因编码框、转酮酶基因编码框的质粒pRS-RKI1-TKL1图谱。Fig. 3 is a map of plasmid pRS-RKI1-TKL1 containing ribose phosphate isomerase gene coding frame and transketolase gene coding frame.
图4是含有戊糖磷酸差向异构酶基因编码框、转醛酶基因编码框的质粒pAUR-RPE1-TAL1图谱。Fig. 4 is a map of the plasmid pAUR-RPE1-TAL1 containing the coding frame of the pentose phosphate epimerase gene and the coding frame of the transaldolase gene.
图5为菌株L2612PR、L2612PR-DPPP、SyBE005在含有20g/L木糖的发酵培养基中发酵时木糖利用情况。Fig. 5 shows the utilization of xylose when the strains L2612PR, L2612PR-DPPP and SyBE005 were fermented in the fermentation medium containing 20 g/L xylose.
图6为菌株L2612PR、L2612PR-DPPP、SyBE005在含有20g/L木糖的发酵培养基中发酵时乙醇产生情况。Figure 6 shows the production of ethanol by strains L2612PR, L2612PR-DPPP, and SyBE005 when they were fermented in a fermentation medium containing 20 g/L xylose.
图7为菌株L2612PR、L2612PR-DPPP、SyBE005在含有20g/L木糖的发酵培养基中发酵时木糖醇产生情况。Fig. 7 shows the production of xylitol when the strains L2612PR, L2612PR-DPPP, and SyBE005 were fermented in a fermentation medium containing 20 g/L xylose.
具体实施方式Detailed ways
下面结合具体实施例对本发明作进一步的说明,本发明的实施例是为了使本领域的技术人员能够更好地理解本发明,但不对本发明做任何限制。The present invention will be further described below in conjunction with specific examples. The examples of the present invention are intended to enable those skilled in the art to better understand the present invention, but do not limit the present invention in any way.
实施例1Example 1
重组酵母菌株SyBE005的构建与筛选Construction and Screening of Recombinant Yeast Strain SyBE005
出发菌株:出发菌株L2612,是美国威斯康星大学麦迪逊分校的Thomas Jeffries教授赠予,基因型是MAT alpha,leu2,ura3,trp1。是亮氨酸、尿嘧啶和色氨酸缺陷。Starting strain: The starting strain L2612 was donated by Professor Thomas Jeffries of the University of Wisconsin-Madison in the United States, and the genotype is MAT alpha, leu2, ura3, trp1. It is deficient in leucine, uracil and tryptophan.
培养基culture medium
筛选培养基A:合成氮源YNB6.7g/L,混合氨基酸粉末2g/L(具体配方参考[美]D.C.安伯格等酵母遗传学方法试验指南),亮氨酸100mg/L,色氨酸100mg/L,葡萄糖20g/L。Screening medium A: Synthetic nitrogen source YNB6.7g/L, mixed amino acid powder 2g/L (refer to [US] D.C. Amberg et al. Yeast Genetics Method Test Guide for specific formula), leucine 100mg/L, tryptophan 100mg/L, glucose 20g/L.
筛选培养基B:合成氮源YNB6.7g/L,混合氨基酸粉末2g/L,色氨酸100mg/L,葡萄糖20g/L。Screening medium B: synthetic nitrogen source YNB6.7g/L, mixed amino acid powder 2g/L, tryptophan 100mg/L, glucose 20g/L.
筛选培养基C:合成氮源YNB6.7g/L,混合氨基酸粉末2g/L,葡萄糖20g/L。Screening medium C: synthetic nitrogen source YNB6.7g/L, mixed amino acid powder 2g/L, glucose 20g/L.
筛选培养基D:合成氮源YNB6.7g/L,混合氨基酸粉末2g/L,短梗霉素A0.5mg/L,葡萄糖20g/L。驯化培养基:合成氮源YNB6.7g/L,混合氨基酸粉末2g/L,木糖50g/L。Screening medium D: synthetic nitrogen source YNB6.7g/L, mixed amino acid powder 2g/L, aureobasicin A0.5mg/L, glucose 20g/L. Acclimatization medium: synthetic nitrogen source YNB6.7g/L, mixed amino acid powder 2g/L, xylose 50g/L.
固体培养基中,添加20g/L的琼脂。Add 20g/L agar to the solid medium.
出发重组菌株L2612PR-DPPP的构建Construction of Departure Recombinant Strain L2612PR-DPPP
以菌株L2612基因组为模板,克隆出启动子TDH1p、TDH3p、PGK1p,木酮糖激酶基因XKS1(含自身终止子),戊糖磷酸差向异构酶基因RPE1,核糖磷酸异构酶基因RKI1,转酮酶基因TKL1,转醛酶基因TAL1,终止子序列PGK1t。Using the genome of strain L2612 as a template, the promoters TDH1p, TDH3p, and PGK1p, the xylulokinase gene XKS1 (including its own terminator), the pentose phosphate epimerase gene RPE1, the ribose phosphate isomerase gene RKI1, were cloned. Ketolase gene TKL1, transaldolase gene TAL1, terminator sequence PGK1t.
通过融合PCR技术将合成的木糖还原酶基因XR、木糖醇脱氢酶基因XDH分别与启动子PGK1、终止子PGK1t连接,将启动子PGK1与木酮糖激酶基因XKS1连接,然后将三个基因表达框顺次连接到载体YIplac211(购于ATCC)上,形成表达质粒YIplac211-XRXDHXK(图1)。The synthetic xylose reductase gene XR and xylitol dehydrogenase gene XDH were connected with the promoter PGK1 and the terminator PGK1t respectively by fusion PCR technology, and the promoter PGK1 was connected with the xylulokinase gene XKS1, and then the three The gene expression cassette was sequentially connected to the vector YIplac211 (purchased from ATCC) to form the expression plasmid YIplac211-XRXDHXK (Figure 1).
木糖还原酶基因XR序列用SEQ ID NO:1所示。The XR sequence of the xylose reductase gene is shown in SEQ ID NO:1.
木糖醇脱氢酶基因XDH序列用SEQ ID NO:2所示。The xylitol dehydrogenase gene XDH sequence is shown in SEQ ID NO: 2.
将以上构建的木糖醇脱氢酶基因表达框从质粒YIplac211-XRXDHXK上酶切出来,重新克隆到载体pRS305(购于ATCC)上,形成质粒pRS305-XDH(图2)。The xylitol dehydrogenase gene expression cassette constructed above was digested from the plasmid YIplac211-XRXDHXK, and re-cloned into the vector pRS305 (purchased from ATCC) to form the plasmid pRS305-XDH (Figure 2).
利用融合PCR技术构建戊糖磷酸差向异构酶基因表达盒TDH1p-RPE1-PGK1t,转醛酶基因表达盒PGK1p-TAL1-PGK1t,核糖磷酸异构酶基因表达盒PGK1p-RKI1-PGK1t,转酮酶基因表达盒TDH3p-TKL1-PGK1t。将基因表达盒PGK1p-RKI1-PGK1t和TDH3p-TKL1-PGK1t连接到载体pRS304(购于ATCC)上,形成载体pRS-RKI1-TKL1(图3)。将基因表达盒TDH1p-RPE1-PGK1t和基因表达盒PGK1p-TAL1-PGK1t依次连接到载体pAUR101(大连宝生物公司购买),构建载体pAUR-RPE1-TAL1(图4)。Construction of pentose phosphate epimerase gene expression cassette TDH1p-RPE1-PGK1t, transaldolase gene expression cassette PGK1p-TAL1-PGK1t, ribose phosphate isomerase gene expression cassette PGK1p-RKI1-PGK1t, transketone by fusion PCR technology Enzyme gene expression cassette TDH3p-TKL1-PGK1t. The gene expression cassettes PGK1p-RKI1-PGK1t and TDH3p-TKL1-PGK1t were linked to the vector pRS304 (purchased from ATCC) to form the vector pRS-RKI1-TKL1 (Figure 3). The gene expression cassette TDH1p-RPE1-PGK1t and the gene expression cassette PGK1p-TAL1-PGK1t were sequentially connected to the vector pAUR101 (purchased by Dalian Bao Biological Company) to construct the vector pAUR-RPE1-TAL1 (Figure 4).
用限制性内切酶Apa I线性化YIplac211-XRXDHXK,通过醋酸锂法转化菌株L2612,在筛选培养基A上筛选获得重组菌株L2612PR。并在此重组菌株的基础上,用醋酸锂法转化质粒pRS305-XDH,在筛选培养基B上获得重组菌株。用限制性内切酶EcoRI线性化质粒pRS-RKI1-TKL1,用醋酸锂法转化上一步得到的重组菌株,在筛选培养基C上表达获得重组菌株。并在此菌株的基础上,进一步转化用StuI线性化的质粒pAUR-RPE1-TAL1,在筛选培养基D上得到出发重组菌株L2612PR-DPPP。YIplac211-XRXDHXK was linearized with restriction endonuclease Apa I, and strain L2612 was transformed by lithium acetate method, and recombinant strain L2612PR was obtained by screening on selection medium A. And on the basis of the recombinant strain, the plasmid pRS305-XDH was transformed by the lithium acetate method, and the recombinant strain was obtained on the screening medium B. The plasmid pRS-RKI1-TKL1 was linearized with the restriction endonuclease EcoRI, the recombinant strain obtained in the previous step was transformed by the lithium acetate method, and the recombinant strain was obtained by expressing on the screening medium C. And on the basis of this strain, the plasmid pAUR-RPE1-TAL1 linearized with StuI was further transformed, and the starting recombinant strain L2612PR-DPPP was obtained on the screening medium D.
突变菌株SyBE005的构建和筛选Construction and Screening of Mutant Strain SyBE005
将菌株L2612PR-DPPP以初始OD600=0.2接到含50mL驯化培养基的250mL中,30℃、200转/分有氧培养3天。测量培养物的OD600,并以初始OD600=0.2转接到新鲜驯化培养基中,重复培养10次后菌液的OD600保持不变,继续重复培养10次。取少量的菌液,稀释后在驯化培养基的固体平板上涂布培养,获得单菌落菌株。从其中选取菌落尺寸最大的20个菌落,分别接种到含有2mL液体筛选培养基C的15mL试管中,在30℃、200转/分的条件下培养2天。取100μL菌液转接到3mL新鲜发酵培养基A中,在30℃、200转/分的条件下无氧培养。用带有排气针的橡胶塞密封试管口。无氧培养24小时后,测量菌液的OD600、残余木糖含量和代谢产物乙醇、甘油、木糖醇含量。从20株单菌落中获得了一株残余木糖最少的菌株SyBE005。The strain L2612PR-DPPP was placed into 250 mL containing 50 mL acclimation medium at an initial OD 600 =0.2, and aerobically cultured at 30°C and 200 rpm for 3 days. Measure the OD 600 of the culture, and transfer it to the fresh acclimatization medium with the initial OD 600 =0.2. After 10 repeated cultures, the OD 600 of the bacterial liquid remains unchanged, and continue to repeat the culture 10 times. Take a small amount of bacterial solution, spread it on the solid plate of the acclimatization medium after dilution, and obtain a single colony strain. Select 20 colonies with the largest colony size, inoculate them into 15 mL test tubes containing 2 mL of liquid screening medium C, and culture them at 30°C and 200 rpm for 2 days. Take 100 μL of the bacterial liquid and transfer it to 3 mL of fresh fermentation medium A, and culture it anaerobically at 30°C and 200 rpm. Seal the mouth of the test tube with a rubber stopper with a vent needle. After 24 hours of anaerobic culture, the OD 600 , residual xylose content and metabolite ethanol, glycerol and xylitol content of the bacterial solution were measured. A strain SyBE005 with the least residual xylose was obtained from 20 single colonies.
分析方法:Analytical method:
以722型分光光度计在600nm处测定的菌体吸光值(OD600)表征菌体浓度。木糖、乙醇、木糖醇、甘油的浓度用高效液相色谱(Waters1515)测定。色谱柱为Aminex HPX-87H,柱温:65℃;检测器:Waters示差检测器2421,检测器温度是40℃。流动相为5mM硫酸溶液,流速0.6mL/min,进样量为10μL。The cell concentration was characterized by the cell absorbance value (OD 600 ) measured at 600 nm by a 722-type spectrophotometer. The concentrations of xylose, ethanol, xylitol and glycerol were determined by high performance liquid chromatography (Waters1515). Chromatographic column is Aminex HPX-87H, column temperature: 65°C; detector: Waters differential detector 2421, detector temperature is 40°C. The mobile phase was 5 mM sulfuric acid solution, the flow rate was 0.6 mL/min, and the injection volume was 10 μL.
实施例2菌株L2612PR、L2612PR-DPPP与SyBE005的木糖发酵比较Example 2 Comparison of Xylose Fermentation of Bacterial Strains L2612PR, L2612PR-DPPP and SyBE005
1.试验材料:菌株L2612PR、L2612PR-DPPP、SyBE0031. Test materials: strains L2612PR, L2612PR-DPPP, SyBE003
2.试验方法:2. Test method:
种子培养基1:合成氮源YNB6.7g/L,混合氨基酸粉末2g/L,葡萄糖20g/L,亮氨酸100mg/L,色氨酸100mg/L。Seed medium 1: synthetic nitrogen source YNB6.7g/L, mixed amino acid powder 2g/L, glucose 20g/L, leucine 100mg/L, tryptophan 100mg/L.
种子培养基2:合成氮源YNB6.7g/L,混合氨基酸粉末2g/L,葡萄糖20g/L。Seed medium 2: synthetic nitrogen source YNB6.7g/L, mixed amino acid powder 2g/L, glucose 20g/L.
发酵培养基:酵母浸粉10g/L,蛋白胨20g/L,木糖20g/L。Fermentation medium: yeast extract powder 10g/L, peptone 20g/L, xylose 20g/L.
从新鲜的斜面上接一环L2612PR菌落到50mL种子培养基1中。类似的,从新鲜的斜面上接菌落L2612PR-DPPP与SyBE005到50mL种子培养基2中。在30℃、200转/分的条件下培养24小时。以初始菌体浓度OD600=1.0接种到100mL发酵培养基中,在30℃、150转/分条件下培养,发酵60小时。检测菌体浓度、木糖浓度和产物乙醇、木糖醇、甘油的浓度。Pick up a loop of L2612PR colony from a fresh slant and put it into 50 mL seed medium 1. Similarly, colonies L2612PR-DPPP and SyBE005 were inoculated into 50 mL of seed medium 2 from a fresh slant. Cultivate for 24 hours at 30°C and 200 rpm. Inoculate 100 mL of fermentation medium with an initial cell concentration of OD 600 =1.0, culture at 30°C and 150 rpm, and ferment for 60 hours. Detect bacterial cell concentration, xylose concentration and product ethanol, xylitol, glycerin concentration.
3.分析方法:3. Analysis method:
同实施例1。With embodiment 1.
4.试验结果:4. Test results:
图5所示,在48小时内菌株SyBE005已经完全利用了木糖,而菌株L2612PR、L2612PR-DPPP都只利用了约60%的木糖,SyBE005的最大木糖比消耗速率达到0.301g/g干重/h;发酵结束后,L2612PR、L2612PR-DPPP、SyBE005的乙醇产量分别达到了2.02g/L、2.97g/L、6.85g/L。L2612PR、L2612PR-DPPP对应的乙醇得率分别为0.15g/g木糖、0.20g/g木糖,SyBE005的发酵乙醇得率达到0.33g/g木糖,相对于L2612PR、L2612PR-DPPP分别提高了120%和65%,如图6所示;发酵结束后,L2612PR、L2612PR-DPPP、SyBE005的木糖醇含量分别达到了6.24g/L、6.29g/L、2.43g/L。L2612PR、L2612PR-DPPP的木糖醇得率达到0.48g/g木糖、0.42g/g木糖,而SyBE005的木糖醇得率降低为0.12g/g木糖,相对于L2612PR、L2612PR-DPPP降低了3、2.5倍,如图7所示。As shown in Figure 5, the strain SyBE005 has fully utilized xylose within 48 hours, while the strains L2612PR and L2612PR-DPPP have only utilized about 60% of xylose, and the maximum xylose specific consumption rate of SyBE005 reached 0.301g/g dry weight/h; after fermentation, the ethanol yields of L2612PR, L2612PR-DPPP, and SyBE005 reached 2.02g/L, 2.97g/L, and 6.85g/L, respectively. The ethanol yields corresponding to L2612PR and L2612PR-DPPP are 0.15g/g xylose and 0.20g/g xylose respectively, and the fermentation ethanol yield of SyBE005 reaches 0.33g/g xylose, which is higher than that of L2612PR and L2612PR-DPPP respectively. 120% and 65%, as shown in Figure 6; after the fermentation, the xylitol content of L2612PR, L2612PR-DPPP, and SyBE005 reached 6.24g/L, 6.29g/L, and 2.43g/L, respectively. The xylitol yield of L2612PR and L2612PR-DPPP reached 0.48g/g xylose and 0.42g/g xylose, while the xylitol yield of SyBE005 decreased to 0.12g/g xylose, compared to L2612PR and L2612PR-DPPP Reduced by 3, 2.5 times, as shown in Figure 7.
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