酿酒酵母纤维素乙醇统合加工(CBP)的策略及研究进展

木质纤维素乙醇的统合生物加工过程(Consolidated bioprocessing,CBP)是将纤维素酶和半纤维素酶生产、纤维素水解和乙醇发酵过程组合或部分组合,通过一种微生物完成。统合生物加工过程有利于降低生物转化过程的成本,越来越受到研究者的普遍关注。酿酒酵母Saccharomyces cerevisiae是传统的乙醇发酵菌株。介绍了影响外源基因在酿酒酵母中表达水平的因素,纤维素酶和半纤维素酶在酿酒酵母中表达研究进展及利用酿酒酵母统合加工纤维素乙醇的策略。     

鸡尾酒δ整合策略构建表达三类纤维素酶的酿酒酵母工程菌株及初步评价

木质纤维素乙醇具有替代化石燃料的潜力,其生产过程包括生物质预处理、纤维素酶生产、水解和发酵等多个步骤。将纤维素酶生产、水解和发酵组合在一起的统合生物加工过程（consolidated bioprocessing,CBP）由于能降低水解和发酵成本而具有应用于纤维素乙醇生产的潜力,该技术的关键是构建能有效降解纤维素的工程菌株,而构建表达纤维素酶的酿酒酵母即是其中一种选择。采用鸡尾酒多拷贝δ整合的策略将7种纤维素酶基因（Trichoderma reesei cbh1、cbh2和egl2,Aspergillus aculeatus cbh1、egl1和bgl1）表达盒整合至酿酒酵母W303-1A染色体上,经4轮整合筛选得到菌株LA1、LA2、LA3和LA4。对这4个菌株进行纤维素酶活性测定,结果表明从LA1到LA3各种纤维素酶活性呈递增趋势,而LA4的酶活性与LA3的酶活水平相当。对菌株LA3进行酸碱预处理玉米芯料的发酵评价,结果表明：①在外加商品化纤维素酶的情况下,与对照菌株W303-1A和AADY相比,LA3能有效利用纤维素料发酵产醇;②与分步整合的菌株W3相比,发酵性能更优;③培养基中的营养成分影响菌株发酵性能。这些结果表明,鸡尾酒δ整合是一种有效的构建酿酒酵母CBP菌株的方法。     

酿酒酵母人造纤维小体的研究进展简

纤维素乙醇的统合生物加工过程（consolidated bioprocessing,CBP）是将（半）纤维素酶生产、纤维素水解和乙醇发酵过程组合,通过一种微生物完成的生物加工过程。 CBP有利于降低生物转化过程的成本,受到研究者的普遍关注。酿酒酵母（ Saccharomyces cerevisiae）作为传统的乙醇生产菌株,是极具潜力的CBP底盘细胞。纤维小体是某些厌氧微生物细胞表面由纤维素酶系与支架蛋白组成的大分子复合物,它能高效降解木质纤维,在酿酒酵母表面展示纤维小体已成为构建CBP细胞的研究热点。笔者综述了人造纤维小体在酿酒酵母细胞表面展示组装的研究进展,重点阐述了纤维小体各元件的设计和改造,并针对酿酒酵母分泌途径的改造,提出提高人造纤维小体分泌组装的可能性策略。     

酿酒酵母人造纤维小体的研究进展

纤维素乙醇的统合生物加工过程(consolidated bioprocessing,CBP)是将(半)纤维素酶生产、纤维素水解和乙醇发酵过程组合,通过一种微生物完成的生物加工过程。CBP有利于降低生物转化过程的成本,受到研究者的普遍关注。酿酒酵母(Saccharomyces cerevisiae)作为传统的乙醇生产菌株,是极具潜力的CBP底盘细胞。纤维小体是某些厌氧微生物细胞表面由纤维素酶系与支架蛋白组成的大分子复合物,它能高效降解木质纤维,在酿酒酵母表面展示纤维小体已成为构建CBP细胞的研究热点。笔者综述了人造纤维小体在酿酒酵母细胞表面展示组装的研究进展,重点阐述了纤维小体各元件的设计和改造,并针对酿酒酵母分泌途径的改造,提出提高人造纤维小体分泌组装的可能性策略。     

纤维素乙醇统合加工过程中的酵母多酶共展示体系研究进展

利用统合生物加工过程(Consolidated bioprocessing,CBP)生产纤维素乙醇是目前国内外的研究热点。CBP需要一种“集成化”微生物,既能生产水解木质纤维素的多种酶类又能利用水解木质纤维素产生的糖类发酵产乙醇。以酿酒酵母表面展示技术为依托,建立CBP菌株多酶共展示体系的研究主要分为以下两个方向：一是直接将纤维素酶展示在细胞表面,即非复合型纤维素酶体系;另一种是通过表面展示纤维小体(Cellulosome)将纤维素酶间接地锚定在细胞表面,即复合型纤维素酶体系,本文主要从以上两个方向阐述了近几年对于纤维素乙醇生物统合加工过程的研究进展。因纤维小体对纤维素的降解能力比非复合型纤维素酶体系更强,所以其在酿酒酵母细胞表面的组装研究受到越来越多的关注,为了更深入透彻地了解纤维小体的酵母展示技术,文中对纤维小体的结构与功能及其在纤维素乙醇发酵中的应用研究进行重点论述,并对该领域的发展方向进行展望。     

过表达MRP8提高酿酒酵母乙酸耐性及乙醇发酵效率

乙酸是木质纤维素水解液中含量较多的抑制物,因此提高酿酒酵母菌株对乙酸的耐受性有助于提高纤维素乙醇生产效率。本文中,笔者利用基于CRISPR/Cas9系统的基因组编辑技术过表达了酿酒酵母(Saccharomyces cerevisiae)S288c线粒体核糖体蛋白编码基因MRP8,并比较了过表达MRP8的菌株与对照菌株的生长和发酵特性。平板耐性检测发现,MRP8过表达明显提高了菌株的乙酸胁迫耐受性;乙醇发酵结果表明,在4.8 g/L乙酸胁迫条件下,过表达菌株MRP8-3在51 h消耗全部的葡萄糖,发酵时间缩短了25 h,显著优于相同时间的对照菌株。本研究结果为构建高效纤维素乙醇发酵的酿酒酵母菌株提供了新思路。     

酿酒酵母木糖转运基因研究进展

由于对全球变暖等日益严重的环境问题的担忧,生产生物乙醇等清洁能源的技术正受到世界各国越来越多的关注。较之以粮食为原料生产乙醇,木质纤维素生产生物乙醇具有更大的发展潜力,因其来源广泛,廉价且可再生。以木质纤维素生产生物乙醇已经取得长足进步,但仍面临几个主要问题,比如天然酿酒酵母不能利用木糖发酵乙醇,木质纤维素酶成本过高,木质纤维素预处理环节成本高等。已经有基因改造的酵母菌株可以利用戊糖和己糖进行生物乙醇生产。然而,这些菌株对木糖的利用效率很低。这主要是因为酿酒酵母缺乏高效的特异性木糖转运基因,木糖运输依赖已糖转运基因。为了提高木糖利用速度,已有不少方法成功应用于构建重组酵母细胞。现对酵母木糖转运基因的最新研究进展进行简要概述。     

过表达tRNA基因tL(CAA)K提高酿酒酵母乙酸耐受性

乙酸是木质纤维素类生物质水解液中的常见毒性抑制物,选育乙酸耐受性好的酿酒酵母菌株,有利于高效利用木质纤维素类生物质,发酵生产生物燃料和生物基化学品。目前对酿酒酵母抗逆性的研究多集中在转录水平,但对转运RNA (Transfer RNA,tRNA) 在耐受性中的作用研究较少。在对酿酒酵母抗逆性研究过程中发现,一些转运RNA基因在耐受性好的酿酒酵母菌株中转录明显上调。本文深入分析了精氨酸tRNA基因tR(ACG)D和亮氨酸tRNA基因tL(CAA)K过表达对酿酒酵母耐受木质纤维素水解液的影响。结果表明,在4.2 g/L乙酸胁迫条件下进行乙醇发酵时,过表达tL(CAA)K的菌株生长和发酵性能均优于对照酵母菌株,乙醇生产强度比对照菌株提高了29.41%,但过表达tR(ACG)D基因的菌株生长和代谢能力较对照菌株明显降低,体现了不同tRNA的不同调控作用。进一步分析发现,过表达tL(CAA)K的重组酵母菌株乙酸耐受性调控相关基因HAA1、MSN2和MSN4等胁迫耐受性相关转录因子编码基因的转录水平上调。本文的研究为选育高效利用木质纤维素资源进行生物炼制的酵母菌株提供了新的改造策略,也为进一步揭示酿酒酵母tRNA基因表达调控对抗逆性的影响提供了基础。     

MRP8过表达促进重组酿酒酵母外切纤维素酶生产

增强酿酒酵母纤维素酶分泌能力,为提高利用联合生物加工生产纤维素乙醇的效率提供基础。采用CRISPR/Cas9基因组编辑技术,在分泌表达外切纤维素酶CBH1的酿酒酵母Y294中过表达线粒体核糖体蛋白基因MRP8。与对照菌株相比,过表达MRP8重组酵母的胞外CBH1酶活提高了约80%。实时定量PCR结果分析表明,在MRP8过表达突变体中,CBH1转录水平高于对照菌株,但是与蛋白折叠和分泌相关的关键基因转录水平没有明显变化。在刚果红平板和含有衣霉素或二硫苏糖醇的平板上生长没有受到影响。胞内ATP含量和活性氧积累未发现显著差别。本研究表明MRP8过表达促进外切纤维素酶的生产。     

一株降解纤维素放线菌的产纤维素酶基因克隆与表达

【背景】纤维素在自然界中储量丰富,但天然纤维素的难降解性成为广泛应用纤维素资源的壁垒,近年来利用微生物来降解纤维素成为热点研究。【目的】筛选分离得到一株具有降解纤维素功能的放线菌菌株Lb1,通过全基因组测序确定其产纤维素酶关键基因5676,对基因5676进行克隆转化,使其在大肠杆菌中进行表达。【方法】通过基因工程技术将产纤维素基因连接到表达质粒上并导入表达菌株,对其降解纤维素生成葡萄糖的能力进行探究。【结果】将Lb1菌株的16S rRNA基因进行比对,确定菌株Lb1属于链霉菌属,命名为Streptomyces sp. Lb1。成功构建出纤维素酶表达载体,并且导入表达菌株大肠杆菌BL21(DE3),重组菌株的产纤维素酶能力大于空载菌株。【结论】通过基因工程技术成功克隆出产纤维素酶基因,从而表达纤维素酶,为今后利用微生物降解纤维素的大规模应用提供参考。     

Thermotolerant Kluyveromyces marxianus and Saccharomyces cerevisiae strains representing potentials for bioethanol production from Jerusalem artichoke by consolidated bioprocessing

Thermotolerant inulin-utilizing yeast strains are desirable for ethanol production from Jerusalem artichoke tubers by consolidated bioprocessing (CBP). To obtain such strains, 21 naturally occurring yeast strains isolated by using an enrichment method and 65 previously isolated Saccharomyces cerevisiae strains were investigated in inulin utilization, extracellular inulinase activity, and ethanol fermentation from inulin and Jerusalem artichoke tuber flour at 40?°C. The strains Kluyveromyces marxianus PT-1 (CGMCC AS2.4515) and S. cerevisiae JZ1C (CGMCC AS2.3878) presented the highest extracellular inulinase activity and ethanol yield in this study. The highest ethanol concentration in Jerusalem artichoke tuber flour fermentation (200?g?L(-1)) at 40?°C achieved by K. marxianus PT-1 and S. cerevisiae JZ1C was 73.6 and 65.2?g?L(-1), which corresponded to the theoretical ethanol yield of 90.0 and 79.7?%, respectively. In the range of 30 to 40?°C, temperature did not have a significant effect on ethanol production for both strains. This study displayed the distinctive superiority of K. marxianus PT-1 and S. cerevisiae JZ1C in the thermotolerance and utilization of inulin-type oligosaccharides reserved in Jerusalem artichoke tubers. It is proposed that both K. marxianus and S. cerevisiae have considerable potential in ethanol production from Jerusalem artichoke tubers by a high temperature CBP.     

One-pot bioethanol production from cellulose by co-culture of Acremonium cellulolyticus and Saccharomyces cerevisiae

ABSTRACT: BACKGROUND: While the ethanol production from biomass by consolidated bioprocess (CBP) is considered to be the most ideal process, simultaneous saccharification and fermentation (SSF) is the most appropriate strategy in practice. In this study, one-pot bioethanol production, including cellulase production, saccharification of cellulose, and ethanol production, was investigated for the conversion of biomass to biofuel by co-culture of two different microorganisms such as a hyper cellulase producer, Acremonium cellulolyticus C-1 and an ethanol producer Saccharomyces cerevisiae. Furthermore, the operational conditions of the one-pot process were evaluated for maximizing ethanol concentration from cellulose in a single reactor. RESULTS: Ethanol production from cellulose was carried out in one-pot bioethanol production process. A. cellulolyticus C-1 and S. cerevisiae were co-cultured in a single reactor. Cellulase producing-medium supplemented with 2.5 g/l of yeast extract was used for productions of both cellulase and ethanol. Cellulase production was achieved by A. cellulolyticus C-1 using Solka-Floc (SF) as a cellulase-inducing substrate. Subsequently, ethanol was produced with addition of both 10%(v/v) of S. cerevisiae inoculum and SF at the culture time of 60 h. Dissolved oxygen levels were adjusted at higher than 20% during cellulase producing phase and at lower than 10% during ethanol producing phase. Cellulase activity remained 8--12 FPU/ml throughout the one-pot process. When 50--300 g SF/l was used in 500 ml Erlenmeyer flask scale, the ethanol concentration and yield based on initial SF were as 8.7--46.3 g/l and 0.15--0.18 (g ethanol/g SF), respectively. In 3-l fermentor with 50--300 g SF/l, the ethanol concentration and yield were 9.5--35.1 g/l with their yields of 0.12--0.19 (g/g) respectively, demonstrating that the one-pot bioethanol production is a reproducible process in a scale-up bioconversion of cellulose to ethanol. CONCLUSION: A. cellulolyticus cells produce cellulase using SF. Subsequently, the produced cellulase saccharifies the SF, and then liberated reducing sugars are converted to ethanol by S. cerevisiae. These reactions were carried out in the one-pot process with two different microorganisms in a single reactor, which does require neither an addition of extraneous cellulase nor any pretreatment of cellulose. Collectively, the one-pot bioethanol production process with two different microorganisms could be an alternative strategy for a practical bioethanol production using biomass.     

Development of a cellulolytic Saccharomyces cerevisiae strain with enhanced cellobiohydrolase activity

Consolidated bioprocessing (CBP) is a promising technology for lignocellulosic ethanol production, and the key is the engineering of a microorganism that can efficiently utilize cellulose. Development of Saccharomyces cerevisiae for CBP requires high level expression of cellulases, particularly cellobiohydrolases (CBH). In this study, to construct a CBP-enabling yeast with enhanced CBH activity, three cassettes containing constitutively expressed CBH-encoding genes (cbh1 from Aspergillus aculeatus, cbh1 and cbh2 from Trichoderma reesei) were constructed. T. reesei eg2, A. aculeatus bgl1, and the three CBH-encoding genes were then sequentially integrated into the S. cerevisiae W303-1A chromosome via δ-sequence-mediated integration. The resultant strains W1, W2, and W3, expressing uni-, bi-, and trifunctional cellulases, respectively, exhibited corresponding cellulase activities. Furthermore, both the activities and glucose producing activity ascended. The growth test on cellulose containing plates indicated that CBH was a necessary component for successful utilization of crystalline cellulose. The three recombinant strains and the control strains W303-1A and AADY were evaluated in acid- and alkali-pretreated corncob containing media with 5 FPU exogenous cellulase/g biomass loading. The highest ethanol titer (g/l) within 7 days was 5.92 ± 0.51, 18.60 ± 0.81, 28.20 ± 0.84, 1.40 ± 0.12, and 2.12 ± 0.35, respectively. Compared with the control strains, W3 efficiently fermented pretreated corncob to ethanol. To our knowledge, this is the first study aimed at creating cellulolytic yeast with enhanced CBH activity by integrating three types of CBH-encoding gene with a strong constitutive promoter Ptpi.     

Deletion of the GRE3 aldose reductase gene and its influence on xylose metabolism in recombinant strains of Saccharomyces cerevisiae expressing the xylA and XKS1 genes.

Saccharomyces cerevisiae ferments hexoses efficiently but is unable to ferment xylose. When the bacterial enzyme xylose isomerase (XI) from Thermus thermophilus was produced in S. cerevisiae, xylose utilization and ethanol formation were demonstrated. In addition, xylitol and acetate were formed. An unspecific aldose reductase (AR) capable of reducing xylose to xylitol has been identified in S. cerevisiae. The GRE3 gene, encoding the AR enzyme, was deleted in S. cerevisiae CEN.PK2-1C, yielding YUSM1009a. XI from T. thermophilus was produced, and endogenous xylulokinase from S. cerevisiae was overproduced in S. cerevisiae CEN.PK2-1C and YUSM1009a. In recombinant strains from which the GRE3 gene was deleted, xylitol formation decreased twofold. Deletion of the GRE3 gene combined with expression of the xylA gene from T. thermophilus on a replicative plasmid generated recombinant xylose utilizing S. cerevisiae strain TMB3102, which produced ethanol from xylose with a yield of 0.28 mmol of C from ethanol/mmol of C from xylose. None of the recombinant strains grew on xylose.     

Analysis of the stress resistance of commercial wine yeast strains

Alcoholic fermentation is an essential step in wine production that is usually conducted by yeasts belonging to the species Saccharomyces cerevisiae. The ability to carry out vinification is largely influenced by the response of yeast cells to the stress conditions that affect them during this process. In this work, we present a systematic analysis of the resistance of 14 commercial S. cerevisiae wine yeast strains to heat shock, ethanol, oxidative, osmotic and glucose starvation stresses. Significant differences were found between these yeast strains under certain severe conditions, Vitilevure Pris Mouse and Lalvin T73 being the most resistant strains, while Fermiblanc arom SM102 and UCLM S235 were the most sensitive ones. Induction of the expression of the HSP12 and HSP104 genes was analyzed. These genes are reported to be involved in the tolerance to several stress conditions in laboratory yeast strains. Our results indicate that each commercial strain shows a unique pattern of gene expression, and no clear correlation between the induction levels of either gene and stress resistance under the conditions tested was found. However, the increase in mRNA levels in both genes under heat shock indicates that the molecular mechanisms involved in the regulation of their expression by stress function in all of the strains.     

Expression and secretion of Clostridium thermocellum endoglucanase A gene (celA) in different Saccharomyces cerevisiae strains

To develop effective and powerful probiotics, Saccharomyces cerevisiae strains producing cellulolytic enzymes were genetically engineered. Two plasmids were constructed in which the carboxymethyl cellulase (CMCase) gene of Clostridium thermocellum was connected in frame with GAPDH or ADH1 promoter. The resultant plasmids were transformed into various S. cerevisiae host cells, and the expression level and secretion efficiency of the CMCase were examined. The difference in genetic background of host strains did affect significantly the cell growth and expression and secretion levels of CMCase. Irrespective of the nature of the host cells, the ADH1 promoter-employing plasmid showed a greater expression level and plasmid stability than the GAPDH promoter-based plasmid. By the optimal host-vector system, S. cerevisiae SEY2102 harboring pVT-CT1 plasmid (ADH1 promoter), the highest expression level of 277 unit CMCase/L was obtained.     

Establishment of a xylose metabolic pathway in an industrial strain of Saccharomyces cerevisiae

To produce an industrial strain of Saccharomyces cerevisiae that metabolizes xylose, we constructed a rDNA integration vector and YIp integration vector, containing the xylose-utilizing genes, XYL1 and XYL2, which encode xylose reductase (XR) and xylitol dehydrogenase (XDH) from Pichia stipitis, and XKS1, which encodes xylulokinase (XK) from S. cerevisiae, with the G418 resistance gene KanMX as a dominant selectable marker. The rDNA results in integration of multiple copies of the target genes. The industrial stain of S. cerevisiae NAN-27 was transformed with the two integration vectors to produce two recombinant strains, S. cerevisiae NAN-127 and NAN-123. Upon transformation, multiple copies of the xylose-utilizing genes were integrated into the genome rDNA locus of S. cerevisiae. Strain NAN-127 consumed twice as much xylose and produced 39% more ethanol than the parent strain, while NAN-123 consumed 10% more xylose and produced 10% more ethanol than the parent strain over 94 h.