草鱼生长激素基因在毕赤酵母中的表达

将草鱼生长激素基因（cGH）的cDNA亚克隆到酵母表达载体pPIC9K中,经电击转化导入毕赤巴斯德酵母GS115菌株,获得转化子。菌落PCR技术筛选证实cGH已经整合到了酵母染色体上。对重组酵母进行诱导表达,SDS-PAGE和Western印迹分析,结果表明cGH的毕赤巴斯德酵母GS115菌株中获得了高效表达。     

商陆抗病毒蛋白重组子筛选及发酵条件初探

目的：筛选体外高表达商陆抗病毒蛋白的毕赤酵母重组菌株,并摸索其适合的发酵条件。方法：通过电击转化将含有商陆抗病毒蛋白（pokeweed antiviral proteins,PAP）基因的分泌型表达载体PIC9K-P导入到毕赤酵母（Pachia pastoris）GS115菌株中。利用免疫印迹法筛选表达量较高的转化子。在摇瓶发酵水平对重组菌株产PAP条件进行初步研究。结果：高表达PAP的重组菌株在发酵时间为96h,10g/L的甲醇浓度,培养基pH值为6.0～6.4时PAP的表达量较高。结论：免疫印迹法适合用于毕赤酵母高表达重组菌株的筛选,重组毕赤酵母的PAP表达量可高达30mg/L。     

利用游离型表达质粒强化毕赤酵母表达木聚糖酶

巴斯德毕赤酵母是用途广泛的蛋白表达系统。目前用于毕赤酵母的质粒主要以整合型质粒为主,很少见到游离的质粒用于外源基因的表达。文中通过将来源于酵母自身的自主复制序列连接到酵母整合型表达载体pGAP中构成自主复制的游离型表达载体pGAPZαA-PARS,将该载体用于表达木聚糖酶基因。转化毕赤酵母后同传统的整合型表达菌株相比,以甘油为碳源时最高酶活达到343 U/mL,比整合型表达提高了45.9%。同时游离载体表达重组酶比活相对整合表达提高了81.2%。为了节约发酵成本,进一步研究了分别以甘油、葡萄糖、蔗糖、混合碳源(蔗糖︰甘油=1︰2)等不同碳源下游离型重组菌株的表达水平。发现甘油表达水平最高,蔗糖最低,但是以工业葡萄糖为碳源时产酶成本最低。由于pGAP载体不需要以甲醇为碳源,因而文中所构建的游离载体pGAPZαA-PARS极大促进了毕赤酵母在食品行业中的应用。同时,游离型载体可大幅度提高表达水平,为进一步研究提高GAP启动子的高效表达奠定了基础。     

产甘油假丝酵母胞浆3-磷酸甘油脱氢酶基因（CgGPD）功能分析

【目的】从高产甘油生产菌株产甘油假丝酵母（Candida glycerinogenes）基因组中克隆了NAD+依赖3-磷酸甘油脱氢酶编码基因（CgGPD）,但是该基因及其上游调控序列具体的功能还是未知的。本文研究了CgGPD基因及其上游调控序列的功能。【方法】本文以酿酒酵母（Saccharomyces cerevisiae）及其渗透压敏感型突变株为宿主,构建3种不同的酵母表达载体导入酵母细胞,研究了不同酵母转化子在渗透压胁迫条件下CgGPD基因表达对细胞的耐高渗透压胁迫应答及其细胞的甘油合成能力的影响。【结果】实验结果表明无论是以来源于S. cerevisiae 的TPI启动子还是来源于CgGPD基因的启动子,过量表达CgGPD基因的转化子均能够显著加速葡萄糖消耗速度和提高甘油合成能力,在gpd1/gpd2突变株中表达CgGPD基因能够消除细胞对外界高渗透压的敏感性,同时转化子胞内甘油大量积累。【结论】CgGPD基因在野生型酵母S. cerevisiae W303-1A表达显著提高细胞的甘油合成能力,在gpd/1gpd2突变株中能够互补GPD1基因的功能,CgGPD基因表达受渗透压诱导 调控。     

里氏木霉内切葡萄糖苷酶Ⅳ在毕赤酵母中的表达

进行了内切葡萄糖苷酶Ⅳ（EGⅣ）在毕赤酵母（Pichia pastoris）表达系统中的表达。采用RT—PCR的方法从里氏木霉（Trichoderma reesei）中分离到eg4基因。将eg4基因与毕赤酵母表达载体pPICZαA连接,得到重组质粒pPICZαA-eg4。将该重组质粒线性化后转化毕赤酵母GS115,eg4基因通过同源重组被整合到毕赤酵母的染色体上,并处于酵母α因子的下游,得到重组菌株P.pastoris—EGⅣ1。在甲醇诱导下,重组菌株P.pastoris-EGⅣ1可以合成并分泌EGⅣ,培养液的CMC活力达到2．11U／mL。     

莱茵衣藻ω-3脂肪酸脱氢酶基因在毕赤酵母中的表达与活性分析

采用RT-PCR方法克隆到莱茵衣藻ω-3脂肪酸脱氢酶基因lyd(l)5,与毕赤酵母表达载体pPIC3.5K连接,电击法转化毕赤酵母GS115.转化子经高浓度G418筛选出高抗性重组子,经PCR鉴定目的基因已整合入毕赤酵母基因组中.甲醇诱导表达,RT-PCR检测表明莱茵表藻ω-3脂肪酸脱氢酶基因在毕赤酵母中得到了表达;毕赤酵母总脂肪酸甲酯经气相色谱(GC)分析结果显示亚油酸的含量明显降低,而α-亚麻酸的含量有所提高.     

利用毕赤酵母系统高效表达灵芝中的免疫调节因子LZ-8蛋白

根据Murasugi等发表的LZ-8基因的DNA序列,利用PCR方法从灵芝菌丝体的基因组DNA中扩增到lz-8基因.将该基因构建到毕赤酵母表达载体上,电激转化毕赤酵母.对转化子先后进行PCR和PCR-Southem鉴定,表明lz-8基因已转入毕赤酵母.转化子经发酵培养后用SDS-PAGE电泳方法检测发酵液,证明毕赤酵母...     

利用毕赤酵母系统表达重组人生长激素的研究

为了获得重组人生长激素在毕赤酵母中高表达的菌株,按毕赤酵母基因密码子偏爱性,人工合成hGH的全基因序列.该基因被克隆到穿梭质粒pPIC9K中,PEG1000介导转入毕赤酵母GS115细胞,通过G418筛选获得高拷贝转化子.在甲醇的诱导下.实现了hGH在毕赤酵母中的成功表达.通过发酵条件的优化.发酵上清中的表达量达1537 mg/L经过超滤和两步层析,重组蛋白的得率这35%,纯度为97%,相对分子质量测定表明重组蛋白的相对分子质量与理论值相近.N-端氨基酸测序证实hGH基因在毕赤酵母中获得正确的表达.     

产肌醇毕赤酵母细胞工厂的优化

【背景】肌醇是一种B族维生素,广泛应用于食品、医药、饲料等领域。微生物发酵法是最具前景的肌醇生产方法,但使用大肠杆菌生产的肌醇在食品及医药领域中的使用受到限制。毕赤酵母作为生物安全菌株是工业上生产异源蛋白的良好宿主,其本身含有天然的肌醇合成途径,具有被改造成为高效生产肌醇细胞工厂的潜力。【目的】通过代谢工程改造毕赤酵母工程菌株,降低副产物的生成并提高肌醇的产量。【方法】以实验室前期构建的产肌醇毕赤酵母工程菌株为出发菌株,确定副产物阿拉伯糖醇、核糖醇和甘露糖合成相关基因。通过关键基因敲除、发酵液中葡萄糖浓度控制降低副产物的产量。通过过表达甘油转运蛋白、甘油激酶和甘油-3-磷酸脱氢酶基因实现产肌醇毕赤酵母对甘油和葡萄糖的共利用,得到重组菌Z10。经过发酵条件优化,进一步提高Z10的肌醇产量。【结果】在最优条件下,重组菌Z10的肌醇产量达到36.7 g/L,是目前酵母类细胞工厂生产肌醇的最高值,副产物总产量与出发菌株相比降低了63.1%。【结论】在毕赤酵母中建立了降低阿拉伯糖醇、核糖醇和甘露糖合成的有效策略,并通过甘油、葡萄糖共利用及相对应的发酵条件优化提高了肌醇产量,为肌醇及其他高价值生物...     

血红蛋白基因在产CBHⅡ毕赤酵母工程菌中的表达

目的:提高毕赤酵母工程菌P.pastoris-CBHⅡ液体发酵产纤维二糖水解酶(CBHⅡ)的能力。方法:分别构建了用于胞外及胞内表达透明颤菌血红蛋白(VHb)基因的毕赤酵母重组表达质粒pPICZαA-vhb与pPICZαA(-s)-vhb。通过电转化将两种质粒转化巴氏毕赤酵母重组菌体P.pastoris-CBHⅡ菌株,经过筛选分别获得可正确表达具有生物活性的VHb蛋白的重组菌株P.pastoris-CBHⅡ-vhb(胞内表达VHb)及P.pastoris-CBHⅡ-vhb(-s)(胞外表达VHb)。结果:摇瓶发酵实验表明,血红蛋白在贫氧条件下可促进CBHⅡ的分泌表达,培养液上清的CMC酶活分别从出发菌株P.pastoris-CBHⅡ的1.81U/ml提高到2.04U/ml(胞内表达VHb)与1.93U/ml(胞外表达VHb)。VHb蛋白胞内表达菌株比胞外表达菌株效果更明显。     

Heterologous expression of Zygosaccharomyces rouxii glycerol 3-phosphate dehydrogenase gene (ZrGPD1) and glycerol dehydrogenase gene (ZrGCY1) in Saccharomyces cerevisiae

We examined the effects of heterologous expression of the open reading frames (ORF) of two genes on salt tolerance and glycerol production in a Saccharomyces cerevisiae strain deficient in glycerol synthesis (gpd1Deltagpd2Delta). When the ORF of the Zygosaccharomyces rouxii glycerol 3-phosphate dehydrogenase gene (ZrGPD1) was expressed under the control of the GAL10 promoter, salt tolerance and glycerol production increased; when the ORF of the glycerol dehydrogenase gene (ZrGCY1) was expressed under the control of the GAL1 promoter, no such changes were observed. Zrgcy1p had a weak effect on glycerol production. These results suggest that Zrgpd1p is the primary enzyme involved in Z. rouxii glycerol production, following a mechanism similar to that of S. cerevisiae (Gpd1p). When the ORFs of the S. cerevisiae glycerol 3-phosphatase gene (GPP2) and ZrGPD1 were simultaneously expressed, glycerol production increased, compared with that in yeast expressing only ZrGPD1.     

产甘油假丝酵母产甘油关键酶基因在酿酒酵母中的表达

甘油是一种极其理想的耐高渗透压介质。利用PCR方法,从产甘油假丝酵母WL2002-5中扩增出了2个产甘油的关键酶基因GPD和GPP,分别编码3-磷酸甘油脱氢酶（glycerol 3-phosphate dehydrogenase, GPD）和3-磷酸甘油磷酸酶（glycerol 3-phosphate phosphatase, GPP）。利用T-Vector在Escherichia coli JM109中克隆得到大量的GPD和GPP基因,并成功构建了重组质粒pYX212-GPD和pYX212-GPP;通过LiAc转化法将重组质粒导入酿酒酵母Saccharomyces cerevisiae W303-1A。初步实验结果表明：发酵过程中pYX212-GPD/S. cerevisiae W303-1A的生物量高于pYX212-GPP/S. cerevisiae W303-1A和野生型S. cerevisiae W303-1A;发酵72h后,pYX212 GPD/S. cerevisiae W303-1A发酵液中甘油含量大约为12mmol/L,明显高于野生型S. cerevisiae W303-1A的甘油含量,而pYX212-GPP/S. cerevisiae W303-1A与野生型S. cerevisiae W303-1A在甘油含量上相差不大,均只有4mmol/L 左右。     

Heterologous Expression of Glycerol 3-Phosphate Dehydrogenase Gene [DhGPD1] from the Osmotolerant Yeast Debaryomyces hansenii in Saccharomyces cerevisiae

The role for the gene encoding glycerol 3-phosphate dehydrogenase (DhGPD1) from the osmotolerant yeast Debaryomyces hansenii, in glycerol production and halotolerance, was studied through its heterologous expression in a Saccharomyces cerevisiae strain deficient in glycerol synthesis (gpd1Δ). The expression of the DhGPD1 gene in the gpd1Δ background restored glycerol production and halotolerance to wild type levels, corroborating its role in the salt-induced production of glycerol. Although the gene was functional in S. cerevisiae, its heterologous expression was not efficient, suggesting that the regulatory mechanism may not be shared by these two yeasts.     

Study of two-stage processes for the microbial production of 1,3-propanediol from glucose

The microbial production of 1,3-propanediol (1,3-PD) from glucose was studied in a two-stage fermentation process on a laboratory scale. In the first stage, glucose was converted to glycerol either by the osmotolerant yeast Pichia farinosa or by a recombinant Escherichia coli strain. In the second stage, glycerol in the broth from the first stage was converted to 1,3-PD by Klebsiella pneumoniae. The culture broth from P. farinosa was shown to contain toxic metabolites that strongly impair the growth of K. pneumoniae and the formation of 1,3-PD. Recombinant E. coli is more suitable than P. farinosa for producing glycerol in the first stage. The fermentation pattern from glycerol can be significantly altered by the presence of acetate, leading to a significant reduction of PD yield in the second stage. However, in the recombinant E. coli culture acetate formation can be prevented by fed-batch cultivation under limiting glucose supply, resulting in an effective production of 1,3-PD in the second stage with a productivity of 2.0 g l(-1) h(-1) and a high yield (0.53 g/g) close to that of glycerol fermentation in a synthetic medium. The overall 1,3-PD yield from glucose in the two stage-process with E. coli and K. pneumoniae reached 0.17 g/g.     

Cloning of the glycerol kinase gene of Bacillus subtilis

A 3.5 kb fragment of Bacillus subtilis DNA which contains wild type alleles of mutations in glpK (glycerol kinase) and glpD (glycerol-3-phosphate [G3P] dehydrogenase) was cloned in plasmid pHV32 in Escherichia coli. The cloned fragment expresses glycerol kinase in B. subtilis mutants carrying the mutations glpK11 and recE4 after induction with glycerol or G3P whereas it does not express G3P dehydrogenase. The cloned fragment thus contains the complete glpK but probably only part of glpD.     

Overexpressing <Emphasis Type="Italic">GLT1</Emphasis> in <Emphasis Type="Italic">gpd1</Emphasis>Δ mutant to improve the production of ethanol of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

To improve ethanol production in Saccharomyces cerevisiae, two yeast strains were constructed. In the mutant, KAM-4, the GPD1 gene, which encodes a glycerol 3-phosphate dehydrogenase of S. cerevisiae to synthesize glycerol, was deleted. The mutant KAM-12 had the GLT1 gene (encodes glutamate synthase) placed under the PGK1 promoter while harboring the GPD1 deletion. Notably, overexpression of GLT1 by the PGK1 promoter along with GPD1 deletion resulted in a 10.8% higher ethanol production and a 25.0% lower glycerol formation compared to the wild type in anaerobic fermentations. The growth rate of KAM-4 was slightly lower than that of the wild type under the exponential phase whereas KAM-12 and the wild type were indistinguishable in the biomass concentration at the end of growth period. Meanwhile, dramatic reduction of formation of acetate and pyruvic acid was observed in all the mutants compared to the wild type.     

Genetic determinants for enhanced glycerol growth of Saccharomyces cerevisiae

The yeast Saccharomyces cerevisiae generally shows a low natural capability to utilize glycerol as the sole source of carbon, particularly when synthetic medium is used and complex supplements are omitted. Nevertheless, wild type isolates have been identified that show a moderate growth under these conditions. In the current study we made use of intraspecies diversity to identify targets suitable for reverse metabolic engineering of the non-growing laboratory strain CEN.PK113-1A. A genome-wide genetic mapping experiment using pooled-segregant whole-genome sequence analysis was conducted, and one major and several minor genetic loci were identified responsible for the superior glycerol growth phenotype of the previously selected S. cerevisiae strain CBS 6412-13A. Downscaling of the major locus by fine-mapping and reciprocal hemizygosity analysis allowed the parallel identification of two superior alleles (UBR2_{CBS 6412-13A} and SSK1_{CBS 6412-13A}). These alleles together with the previously identified GUT1_{CBS 6412-13A} allele were used to replace the corresponding alleles in the strain CEN.PK113-1A. In this way, glycerol growth could be established reaching a maximum specific growth rate of 0.08 h⁻¹. Further improvement to a maximum specific growth rate of 0.11 h⁻¹ could be achieved by heterologous expression of the glycerol facilitator FPS1 from Cyberlindnera jadinii.     

Glycerol metabolism in the methylotrophic yeast Hansenula polymorpha: phosphorylation as the initial step

In hansenula polymorpha glycerol is metabolized via glycerol kinase and NAD(P)-independent glycerol-3-phosphate (G3P) dehydrogenase, enzymes which hitherto were reported to be absent in this methylotrophic yeast. Activity of glycerol kinase was readily detectable when cell-free extracts were incubated at pH 7–8 with glycerol/ATP/Mg²⁺ and a discontinuous assay for G3P formation was used. This glycerol kinase activity could be separated from dihydroxyacetone (DHA) kinase activity by ion exchange chromatography. Glycerol kinase showed relatively low affinities for glycerol (apparent K _m=1.0 mM) and ATP (apparent K _m=0.5 mM) and was not active with other substrates tested. No inhibition by fructose-1,6-bisphosphate (FBP) was observed. Both NAD-dependent and NAD(P)-independent G3P dehydrogenases were present. The latter enzyme could be assayed with PMS/MTT and cosedimented with the mitochondrial fraction. Glucose partly repressed synthesis of glycerol kinase and NAD(P)-independent G3P dehydrogenase, but compared to several other non-repressing carbon sources no clear induction of these enzymes by glycerol was apparent. Amongst glycerolnegative mutants of H. polymorpha strain 17B (a DHA kinase-negative mutant), strains blocked in either glycerol kinase or membrane-bound G3P dehydrogenase were identified. Crosses between representatives of the latter mutants and wild type resulted in the isolation of, amongst others, segregants which had regained DHA kinase but were still blocked in the membrane-bound G3P dehydrogenase. These strains, employing the oxidative pathway, were only able to grow very slowly in glycerol mineral medium.Abbreviations DHA dihydroxyacetone - G3P glycerol-3-phosphate - EMS ethyl methanesulphonate - MTT 3-(4,5-dimethyl-thiazolyl-2)-2,5-diphenyl tetrazolium bromide - PMS phenazine methosulphate - FBP fructose-1,6-bisphosphate     

Engineering of a Glycerol Utilization Pathway for Amino Acid Production by Corynebacterium glutamicum

The amino acid-producing organism Corynebacterium glutamicum cannot utilize glycerol, a stoichiometric by-product of biodiesel production. By heterologous expression of Escherichia coli glycerol utilization genes, C. glutamicum was engineered to grow on glycerol. While expression of the E. coli genes for glycerol kinase (glpK) and glycerol 3-phosphate dehydrogenase (glpD) was sufficient for growth on glycerol as the sole carbon and energy source, additional expression of the aquaglyceroporin gene glpF from E. coli increased growth rate and biomass formation. Glutamate production from glycerol was enabled by plasmid-borne expression of E. coli glpF, glpK, and glpD in C. glutamicum wild type. In addition, a lysine-producing C. glutamicum strain expressing E. coli glpF, glpK, and glpD was able to produce lysine from glycerol as the sole carbon substrate as well as from glycerol-glucose mixtures.     

A modular metabolic engineering approach for the production of 1,2-propanediol from glycerol by Saccharomyces cerevisiae

Compared to sugars, a major advantage of using glycerol as a feedstock for industrial bioprocesses is the fact that this molecule is more reduced than sugars. A compound whose biotechnological production might greatly profit from the substrate's higher reducing power is 1,2-propanediol (1,2-PDO). Here we present a novel metabolic engineering approach to produce 1,2-PDO from glycerol in S. cerevisiae. Apart from implementing the heterologous methylglyoxal (MG) pathway for 1,2-PDO formation from dihydroxyacetone phosphate (DHAP) and expressing a heterologous glycerol facilitator, the employed genetic modifications included the replacement of the native FAD-dependent glycerol catabolic pathway by the 'DHA pathway' for delivery of cytosolic NADH and the reduction of triosephosphate isomerase (TPI) activity for increased precursor (DHAP) supply. The choice of the medium had a crucial impact on both the strength of the metabolic switch towards fermentation in general (as indicated by the production of ethanol and 1,2-PDO) and on the ratio at which these two fermentation products were formed. For example, virtually no 1,2-PDO but only ethanol was formed in synthetic glycerol medium with urea as the nitrogen source. When nutrient-limited complex YG medium was used, significant amounts of 1,2-PDO were formed and it became obvious that the concerted supply of NADH and DHAP are essential for boosting 1,2-PDO production. Additionally, optimizing the flux into the MG pathway improved 1,2-PDO formation at the expense of ethanol. Cultivation of the best-performing strain in YG medium and a controlled bioreactor set-up resulted in a maximum titer of > 4 g L⁻¹ 1,2-PDO which, to the best of our knowledge, has been the highest titer of 1,2-PDO obtained in yeast so far. Surprisingly, significant 1,2-PDO production was also obtained in synthetic glycerol medium after changing the nitrogen source towards ammonium sulfate and adding a buffer.