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。     

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。     

纤维素酶在酿酒酵母中的表达研究

统合生物加工过程（Consolidated bioprocessing,CBP）具有应用于纤维素乙醇生产的潜力,而该技术的关键是构建能有效降解纤维素的工程菌株。酿酒酵母是传统的乙醇发酵菌株,作为CBP宿主菌株具有很多优势,因此在酿酒酵母中表达纤维素酶引起研究者的普遍关注。综述了纤维素酶基因在酿酒酵母中表达的影响因素,包括基因表达盒表达元件（启动子、信号肽和终止子等）、纤维素酶基因拷贝数及存在形式以及纤维素酶基因来源等,并对一种和多种纤维素酶基因在酿酒酵母中的表达及构建得到的CBP菌株研究进展做了简要介绍。     

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。     

纤维小体在燃料乙醇中的应用

纤维小体在木质纤维素的降解中起着重要作用。它不仅含有降解纤维素所需的各种纤维素酶系,而且组装成具有高效催化活性的多酶复合体形式。介绍了纤维小体基本结构与功能,重点概述了其在生物燃料乙醇中的应用并对纤维小体的研究提出了展望。     

降解纤维素的“超分子机器”研究进展

综述了目前关于纤维小体组装模式、纤维小体结构多样性及人工设计纤维小体等方面的研究进展.纤维小体是某些厌氧菌产生的由多个亚基共同组装而成的大分子机器,是致力于组织、协调多种酶组分协同高效催化降解木质纤维素的胞外蛋白质复合体.纤维小体是厌氧微生物水解纤维素的主体,具有非常高效的打破结晶纤维素的结晶结构和降解纤维素链的作用.纤维小体对木质纤维素降解的高效性来自于其自发组装而成的复杂的高级结构,其结构的复杂性因不同的厌氧微生物而有所不同.     

典型产纤维小体梭菌的遗传改造及其在纤维素乙醇中的应用研究进展简

以解纤维梭菌（ Clostridium cellulolyticum）和热纤梭菌（ Clostridium thermocellum）为代表的产纤维小体梭菌可以直接完成从木质纤维素原料到乙醇的生物转化,是用于通过整合生物加工技术生产纤维素乙醇的优良候选菌株。然而,这些产纤维小体梭菌的纤维素降解效率及乙醇产量尚不能满足工业化生产的要求,其遗传改造技术的不成熟严重制约了通过定向代谢工程改造提高生产性能的进程。针对这些典型的产纤维小体菌株,各国科学家近年来在基于二类内含子的嗜中温及嗜高温遗传改造平台建立方面取得了较大突破,并通过靶向代谢工程改造,显著提高纤维素乙醇的产量。笔者对这些前期研究工作以及国内外相关研究成果进行系统的总结,并对构建的遗传改造工具的应用前景进行展望。     

利用Flo1p锚定蛋白在酿酒酵母表面展示三种纤维素酶的纤维素乙醇发酵

为了简化纤维素乙醇生产工艺,实现纤维素利用与乙醇发酵的同步进行,通过酵母细胞表面展示技术,以酿酒酵母菌株Saccharomyces cerevisiae Y5为受体,通过絮凝素(Flo1p)锚定方式,将来自丝状真菌里氏木霉Trichoderma reesei的内切葡聚糖酶Ⅱ(EGII)、纤维二糖水解酶Ⅱ(CBHII)以及来自棘孢曲霉Aspergillus aculeatus的β-葡糖苷酶Ⅰ(BGLI)展示在细胞表面,构建同时表达3种纤维素酶的酵母菌群系统。经过免疫荧光验证展示酶的细胞蛋白定位,酶活测定,乙醇发酵性能验证,结果表明:展示表达的3种纤维素酶具有良好的稳定性和功能活性;在EGII、CBHII和BGLI协同作用下重组酵母菌株能够水解溶胀磷酸纤维素(Phosphoric acid swollen cellulose,简称PASC)并产生乙醇,乙醇浓度达到最大值0.77 g/L,乙醇产量为0.35 g/g,相当于理论值的68.6%。本研究成功构建了利用Flo1p作为锚定蛋白的絮凝素展示系统,初步实现了纤维素利用与乙醇发酵的同步进行,为利用酿酒酵母表面展示技术固定并表达纤维素酶提供了一定的理论依据。     

微生物降解利用木质纤维素的协同作用

木质纤维素复杂的结构组成,是制约高效降解利用这一资源、发展生物炼制的瓶颈。微生物的多酶(菌)体系可有效降解木质纤维素。除好氧微生物的游离酶协同系统之外,主要存在于厌氧细菌中的纤维小体也是有序、高效的协同降解纤维素的复合体系。近年来,在天然纤维小体研究的基础上,研究者们成功设计、构建了人工纤维小体,加深了对这一复合体系的组成单元的理性认识。另外,菌群共培养技术利用各组成菌株代谢途径的协同作用实现了木质纤维素的高效降解。最后,引入异源纤维素酶,可改造现有工程菌株的代谢网络,提高工程菌发酵生产终产物的能力。这些技术有利于实现一步转化生产乙醇的联合生物工艺,有助于提高生物炼制的产率、降低生产成本。     

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.     

Consolidated bioprocessing and simultaneous saccharification and fermentation of lignocellulose to ethanol with thermotolerant yeast strains

Consolidated bioprocessing (CBP), which integrates enzyme production, saccharification and fermentation into a single process, is a promising strategy for effective ethanol production from lignocellulosic materials because of the resulting reduction in utilities, the substrate and other raw materials and simplification of operation. CBP requires a highly engineered microbial strain capable of hydrolyzing biomass with enzymes produced on its own and producing high-titer ethanol. Recently, heterologous production of cellulolytic enzymes has been pursued with yeast hosts, which has realized direct conversion of cellulose to ethanol. Specifically, the development of cell surface engineering, which provides a display of cellulolytic enzymes on the yeast cell surface, facilitates effective biomass hydrolysis concomitantly with ethanol production. On the other hand, the difference in optimum temperature between saccharification and fermentation is a drawback of efficient ethanol production in the simultaneous saccharification and fermentation (SSF). The application of thermotolerant yeast strains engineered to the SSF process would overcome the drawback by performing hydrolysis and fermentation at elevated temperature. In this review, we focus on the recent advances in the application of thermotolerant yeast to CBP and SSF of lignocellulosic material to ethanol. The development of thermotolerant and ethanologenic yeast strains with the ability to hydrolyze lignocellulosic materials is emphasized for high-temperature CBP.     

兼性厌氧复合菌群H纤维素降解和产乙醇能力及生态组成初探

通过限制性培养条件和连续继代培养,筛选获得了一组具有高效稳定降解纤维素能力的复合菌群H。该菌群在传代30代以上仍能保持各项性状稳定,其工作pH为6～9,3 d可以完全降解置于100 mL PCS缓冲液培养基中的滤纸,发酵液中能够检出1.54 g/L乙醇。通过16S rDNA扩增和DGGE的方法,对菌群在不同阶段的微生物组成进行了研究,确定了琥珀酸嗜热梭菌Clostridium thermo succinogene、产气荚膜梭菌Clostridium straminisolvens和紫色板蓝根梭菌Clostridium isatidis等多种可直接实现纤维素到乙醇转化的菌株。菌群通过菌种之间的协同作用,共同维持了体系的稳定及降解能力的稳定。明确菌系的组成,对于进一步研究菌群降解机理、优化菌群和提高乙醇产率意义重大。     

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.     

Surface display of a functional minicellulosome by intracellular complementation using a synthetic yeast consortium and its application to cellulose hydrolysis and ethanol production

In this paper, we report the surface assembly of a functional minicellulosome by using a synthetic yeast consortium. The basic design of the consortium consisted of four different engineered yeast strains capable of either displaying a trifunctional scaffoldin, Scaf-ctf (SC), carrying three divergent cohesin domains from Clostridium thermocellum (t), Clostridium cellulolyticum (c), and Ruminococcus flavefaciens (f), or secreting one of the three corresponding dockerin-tagged cellulases (endoglucanase [AT], exoglucanase [EC/CB], or β-glucosidase [BF]). The secreted cellulases were docked onto the displayed Scaf-ctf in a highly organized manner based on the specific interaction of the three cohesin-dockerin pairs employed, resulting in the assembly of a functional minicellulosome on the yeast surface. By exploiting the modular nature of each population to provide a unique building block for the minicellulosome structure, the overall cellulosome assembly, cellulose hydrolysis, and ethanol production were easily fine-tuned by adjusting the ratio of different populations in the consortium. The optimized consortium consisted of a SC:AT:CB:BF ratio of 7:2:4:2 and produced almost twice the level of ethanol (1.87 g/liter) as a consortium with an equal ratio of the different populations. The final ethanol yield of 0.475 g of ethanol/g of cellulose consumed also corresponded to 93% of the theoretical value. This result confirms the use of a synthetic biology approach for the synergistic saccharification and fermentation of cellulose to ethanol by using a yeast consortium displaying a functional minicellulosome.     

Functional Assembly of Minicellulosomes on the Saccharomyces cerevisiae Cell Surface for Cellulose Hydrolysis and Ethanol Production

We demonstrated the functional display of a miniscaffoldin on the Saccharomyces cerevisiae cell surface consisting of three divergent cohesin domains from Clostridium thermocellum (t), Clostridium cellulolyticum (c), and Ruminococcus flavefaciens (f). Incubation with Escherichia coli lysates containing an endoglucanase (CelA) fused with a dockerin domain from C. thermocellum (At), an exoglucanase (CelE) from C. cellulolyticum fused with a dockerin domain from the same species (Ec), and an endoglucanase (CelG) from C. cellulolyticum fused with a dockerin domain from R. flavefaciens (Gf) resulted in the assembly of a functional minicellulosome on the yeast cell surface. The displayed minicellulosome retained the synergistic effect for cellulose hydrolysis. When a β-glucosidase (BglA) from C. thermocellum tagged with the dockerin from R. flavefaciens was used in place of Gf, cells displaying the new minicellulosome exhibited significantly enhanced glucose liberation and produced ethanol directly from phosphoric acid-swollen cellulose. The final ethanol concentration of 3.5 g/liter was 2.6-fold higher than that obtained by using the same amounts of added purified cellulases. The overall yield was 0.49 g of ethanol produced per g of carbohydrate consumed, which corresponds to 95% of the theoretical value. This result confirms that simultaneous and synergistic saccharification and fermentation of cellulose to ethanol can be efficiently accomplished with a yeast strain displaying a functional minicellulosome containing all three required cellulolytic enzymes.Production of bioethanol from biomass has recently attracted attention due to the mandate for a billion gallons of renewable fuel by the new Energy Policy Act (22). Current production processes using sugar cane and cornstarch are well established (19, 23). However, utilization of a cheaper substrate would render bioethanol more competitive with fossil fuel (29). Cellulosic biomass found in many low-value agricultural or wood pulping wastes is particularly well suited because of its large-scale availability, low cost, and environmentally benign production (23). The primary obstacle impeding the more widespread production of ethanol from cellulose is the absence of a low-cost technology for overcoming its recalcitrant nature (21).Recently, a new method known as consolidated bioprocessing (CBP) has been proposed that combines enzyme production, cellulose saccharification, and fermentation into a single process to dramatically reduce the cost of ethanol production (22). An ideal microorganism for CBP should possess the capability of simultaneous cellulose saccharification and ethanol fermentation. One attractive candidate is Saccharomyces cerevisiae, which is widely used for industrial ethanol production due to its high ethanol productivity and high inherent ethanol tolerance (24). Attempts have been made to engineer S. cerevisiae to hydrolyze cellulose (6, 7, 16). However, due to energetic limitations under anaerobic conditions, only a small amount of cellulases can often be secreted. An alternative is to display the cellulolytic enzymes on the yeast cell surface (13, 14). Up to three different cellulases have been displayed, permitting the hydrolysis of cellulose with concomitant ethanol production. While these results point to a potential strategy of combining ethanol-producing capability with cellulose hydrolysis, the efficiency of hydrolysis must be significantly improved before it can be employed for practical applications.Many anaerobic bacteria have developed an elaborately structured enzyme complex on the cell surface, called the cellulosome, to maximize the catalytic efficiency of cellulose hydrolysis with only a limited amount of enzymes (1, 8, 9). The major component of these cellulosome complexes is a structural scaffoldin consisting of at least one cellulose-binding domain (CBD) and repeating cohesin domains, which are docked individually with a different cellulase tagged with the corresponding dockerin domain (26). Since the interaction between dockerin and cohesin is species specific (17, 25), designer minicellulosomes composed of three different dockerin-cohesin pairs with a cellulose hydrolysis efficiency up to sixfold higher than that of similar free enzymes have been generated (11, 12). Recently, it has been shown that the specific cellulose hydrolysis rates of metabolically active cultures of C. thermocellum displaying cellulosomes are more than fourfold higher than those of purified cellulosomes (20). This significant improvement appears to be a surface phenomenon involving adhesion to cellulose for enhanced substrate capture.In the present report, we demonstrate the functional assembly of a minicellulosome composed of three different cellulases on the S. cerevisiae cell surface and the feasibility of using the engineered yeast strains for cellulosic ethanol production. The success of displaying a functional cellulosome on the surface of an organism that already produces high titers of ethanol could lay a foundation for the achievement of an industrially relevant CBP-enabling microorganism.     

Plant cell walls to ethanol

Conversion of plant cell walls to ethanol constitutes second generation bioethanol production. The process consists of several steps: biomass selection/genetic modification, physiochemical pretreatment, enzymatic saccharification, fermentation and separation. Ultimately, it is desirable to combine as many of the biochemical steps as possible in a single organism to achieve CBP (consolidated bioprocessing). A commercially ready CBP organism is currently unreported. Production of second generation bioethanol is hindered by economics, particularly in the cost of pretreatment (including waste management and solvent recovery), the cost of saccharification enzymes (particularly exocellulases and endocellulases displaying kcat ~1?s-1 on crystalline cellulose), and the inefficiency of co-fermentation of 5- and 6-carbon monosaccharides (owing in part to redox cofactor imbalances in Saccharomyces cerevisiae).