我国秸秆生物转化燃料酒精研究现状

重点介绍了我国自主技术开发的秸杆预处理、产酶菌的诱变育种、纤维素酶活性提高技术、酶系组分的现代生物技术应用、酿酒酵母工程菌的构建和发酵工艺、酒精脱水等新技术应用,展望了秸杆生物转化酒精的可能的工业化途径。     

微生物转化稻草、蔗渣产生酒精

利用生物转化纤维素物质生产酒精,已经引起各国有关科学家的普遍重视。最近M. V. Deshpande等(印度)报道:他们把稻草和蔗渣先用2N NaOH在30℃处理48小时脱除木质素,然后再用微生物发酵生产酒精。作者比较了两种转化方法,第一种是把蘑化和酒精发酵分开进行,先用齐整小核菌UV 8在50℃,pH4.5糖种48小时,然后接种酿酒酵母(NCI M3095)在30℃保温一段时间进行酒精发酵。第二种是把糖化和酒精发酵同时进行。在40℃pH4.5糖化/酒精发酵(酿酒酵母NCI M3078)同时进行48小时后再30℃保温一段时间。     

木质素酶及其生产菌的筛选育种

木质素酶降解木质纤维素材料中的木质素,使木质素-半纤维素-纤维素结构解体,纤维素得以暴露出来供后续步骤处理.它广泛应用于生物制浆、生物漂白、废水处理等工业过程中.由于近年利用可再生木质纤维素材料用酶法水解生产酒精成了研究热点,因而作为纤维素材料生物转化工艺预处理过程中的关键角色,木质素酶也极大地唤起人们的研究兴趣.本文介绍了木质素与白腐真菌(Phanerochaete chrysosporium)木质素降解酶系的特征以及锰过氧化物酶、木质素过氧化物酶、漆酶等3种木质素酶的催化作用机理,归纳了目前流行的木质素酶产生菌的筛选方法及近年来从自然界筛选木质素酶高产菌的种类,并对产木质素酶野生菌株的诱变育种与基因工程改造的进展进行了阐述.     

甘油歧化生产1,3-丙二醇过程的代谢和基因调控机理研究进展

用生物转化法将可再生资源(如淀粉、纤维素等)转化为重要的化工原料是目前生物技术领域的一个重要课题。本文以甘油生物转化为1,3丙二醇过程为考察对象,系统综述了该过程代谢和基因调控的研究现状,并对今后的研究提出了一些建议。     

秸秆分层多级转化液体燃料新工艺的研究进展

目前,秸秆主要作为性质单一组分的纤维素原料而采用生物转化法或快速热解法加以利用。生物转化法主要利用纤维素,而利用木质素和半纤维素较困难;快速热解生物质又使部分组分低值利用,而且得到的生物油品质低。为解决单一的生物或热转化方式存在的问题,提出秸秆分层多级转化液体燃料的新构思,即以秸秆“组分分离、分级定向转化”为核心,将生物转化和热转化有机结合多级转化生产燃料酒精与生物油。研究结果表明,秸秆经过汽爆处理后,采用高浓度发酵一分离乙醇耦合系统,可降低纤维素酶用量,提高了纤维素酶解效率,而且简化操作过程,使蒸馏前乙醇浓度达到60％以上。发酵乙醇剩余物再经热解后,不但热解温度较原秸秆明显降低,而且所得生物油品质有了明显改观。     

木质纤维素生物转化产氢技术现状与发展趋势

氢能是一种清洁能源,利用木质纤维素类生物质生产氢气,在生产可再生绿色能源的同时,避免了木质纤维素资源未被充分利用而造成的环境污染和资源浪费,它的开发与应用对人类未来能源与经济发展具有十分重要意义。以下综述了木质纤维素生物转化产氢技术的研究现状,提出了木质纤维素生物转化产氢的总体构想与对产业发展方向的建议。     

低水用量约束条件下的高固体含量纤维乙醇生物加工技术策略

木质纤维素原料生物转化生产纤维乙醇需要使用大量的水和蒸汽,从而使过程能耗和废水排放显著增加,大幅度增加了加工成本。最大限度地降低水和蒸汽用量对过程节能和废水减排并对最终成本控制极为重要。对极限低水用量约束条件下木质纤维素生物转化关键路径进行了实验研究和计算分析,确定了极低水和蒸汽用量的新型预处理技术,实现高效率预处理过程的废水零排放;采用独特的生物脱毒技术,用从自然界筛选的煤油霉菌Amorphotheca resinae ZN1对预处理原料中的抑制物进行了快速生物脱毒;对极限高固体含量下高粘度多相流物系在复杂抑制物胁迫下的酶水解与发酵行为以及放大准则进行了研究;建立了基于Aspen plus平台上的生物质加工物性数据库和严格热力学意义上的全过程流程模拟数学模型,实现了对过程的局部和全局设计与调优。这一综合技术在生物炼制微型工厂中进行了测试,并在纤维素乙醇工业示范装置中得到了应用。该研究结果将为构建具有工业实用价值的节能和清洁化木质纤维素生物转化技术提供依据。     

新书介绍

本书最大新意 新型酶制剂＋生料、低温生产 书中深入具体地阐述了新型酶制剂和酶技术如何对传统酒精生产过程进行改进和提高;关于新的酒精生产过程的介绍,则着重于生料和低温过程。对于从非淀粉类和木质纤维素生产酒精的新领域也有探讨和展望。     

木质纤维素预处理液膜分离脱毒技术研究进展

木质纤维素预处理会产生各种抑制物,严重影响后续的酶水解和微生物发酵。因此,对木质纤维素预处理液进行脱毒处理成为木质纤维素高效经济生物转化的前提条件之一。重点介绍了膜分离技术应用于木质纤维素预处理液的脱毒过程所取得的研究进展。这些膜分离技术包括膜萃取、膜吸附、纳滤、反渗透、电渗析、电去离子、膜电容脱盐、渗透汽化和膜蒸馏等。膜分离技术在木质纤维素预处理液脱毒领域具有十分广阔的应用前景。     

生物转化能源草制取纤维素乙醇的研究进展

随着化石燃料的日益枯竭和环境污染的日益加剧,寻找一种绿色能源以代替化石能源成为当今世界迫在眉睫的任务。清洁燃料当中的生物乙醇具有车用价值,可作为化石能源的替代品而受到研究学者的广泛关注。而草本能源植物的生物转化被认为是生物质能源产业化发展的最有效途径之一。能源草作为木质纤维素原料之一,由于其具有生长快,产量高,抗性强等优势而备受瞩目。详细论述了近期国内外以能源草为底物进行纤维素乙醇的生物转化研究进展,从纤维素原料预处理到乙醇发酵工艺等各方面的进展及存在的问题,并对木质纤维素制取生物质能源的生物转化效率,以及全纤维素组分的多级利用进行了简单阐述,以期找出一条产业化生产纤维素乙醇的最优生产模式。     

Extractive bioconversion in aqueous two-phase systems. A model study on the conversion of cellulose to ethanol

Summary Aqueous two-phase systems composed of dextran and poly (ethylene glycol) have been successfully used for glucose fermentation, cellulose hydrolysis and bioconversion of cellulose to ethanol. The biocatalysts are confined in the bottom phase whereas the products are extracted by the top phase.     

Bioconversion of dilute-acid pretreated sorghum bagasse to ethanol by Neurospora crassa

Bioethanol production from sweet sorghum bagasse (SB), the lignocellulosic solid residue obtained after extraction of sugars from sorghum stalks, can further improve the energy yield of the crop. The aim of the present work was to evaluate a cost-efficient bioconversion of SB to ethanol at high solids loadings (16?% at pretreatment and 8?% at fermentation), low cellulase activities (1-7 FPU/g SB) and co-fermentation of hexoses and pentoses. The fungus Neurospora crassa DSM 1129 was used, which exhibits both depolymerase and co-fermentative ability, as well as mixed cultures with Saccharomyces cerevisiae 2541. A dilute-acid pretreatment (sulfuric acid 2?g/100?g SB; 210?°C; 10?min) was implemented, with high hemicellulose decomposition and low inhibitor formation. The bioconversion efficiency of N. crassa was superior to S. cerevisiae, while their mixed cultures had negative effect on ethanol production. Supplementing the in situ produced N. crassa cellulolytic system (1.0 FPU/g SB) with commercial cellulase and β-glucosidase mixture at low activity (6.0 FPU/g SB) increased ethanol production to 27.6?g/l or 84.7?% of theoretical yield (based on SB cellulose and hemicellulose sugar content). The combined dilute-acid pretreatment and bioconversion led to maximum cellulose and hemicellulose hydrolysis 73.3?% and 89.6?%, respectively.     

Efficacy of a hot washing process for pretreated yellow poplar to enhance bioethanol production

Cost reductions for pretreatment and bioconversion processes are key objectives necessary to the successful deployment of a bioethanol industry. These unit operations have long been recognized for their impact on the production cost of ethanol. One strategy to achieve this objective is to improve the pretreatment process to produce a pretreated substrate resulting in reduced bioconversion time, lower cellulase enzyme usage, and/or higher ethanol yields. Previous research produced a highly digestible pretreated yellow poplar substrate using a multistage, continuously flowing, very dilute sulfuric acid (0.07% (w/v)) pretreatment. This process reduced the time required for the bioconversion of pretreated yellow poplar sawdust to ethanol. This resulted in a substantially improved yield of ethanol from cellulose. However, the liquid volume requirements, steam demand, and complexity of the flow-through reactor configuration were determined to be serious barriers to commercialization of that process. A reconfigured process to achieve similar performance has been developed using a single-stage batch pretreatment followed by a separation of solids and liquids and washing of the solids at a temperatures between 130 and 150 degrees C. Separation and washing at the elevated temperature is believed to prevent a large fraction of the solubilized lignin and xylan from reprecipitating and/or reassociating with the pretreated solids. This washing of the solids at elevated temperature resulted in both higher recovered yields of soluble xylose sugars and a more digestible pretreated substrate for enzymatic hydrolysis. Key operating variables and process performance indicators included acid concentration, temperature, wash volume, wash temperature, soluble xylose recovery, and performance of the washed, pretreated solids in bioconversion via simultaneous saccharification and fermentation (SSF). Initial results indicated over a 50% increase in ethanol yield at 72 h for the hot washed material as compared to the control (no washing, no separation) and a 43% reduction of in the bioconversion time required for a high ethanol yield from cellulose     

乙酸分级预处理甘蔗渣对纤维素酶解性能的影响

为提高甘蔗渣的纤维素酶解性能,采用乙酸脱木素结合碱脱乙酰基的预处理工艺 (Acetoline工艺) 对甘蔗渣进行预处理,考察了乙酸脱木素过程中若干因素对预处理结果的影响,并对预处理后甘蔗渣的纤维素酶解性能进行了研究。结果表明,经过Acetoline预处理后甘蔗渣在7.5％固体含量、15 FPU+10 CBU/g固体的纤维素酶和β-葡萄糖苷酶用量下酶解48 h,酶解聚糖转化率接近80％。与稀酸预处理相比,Acetoline预处理可以得到更高的酶解聚糖转化率。实验结果表明Acetoline工艺是一种可有效提高甘蔗渣纤维素酶解性能的预处理方法。     

Simultaneous Bioconversion of Cellulose and Hemicellulose to Ethanol

ABSTRACT:?

Lignocellulosic materials containing cellulose, hemicellulose, and lignin as their main constituents are the most abundant renewable organic resource present on Earth. The conversion of both cellulose and hemicellulose for production of fuel ethanol is being studied intensively with a view to develop a technically and economically viable bioprocess. The fermentation of glucose, the main constituent of cellulose hydrolyzate, to ethanol can be carried out efficiently. On the other hand, although bioconversion of xylose, the main pentose sugar obtained on hydrolysis of hemicellulose, to ethanol presents a biochemical challenge, especially if it is present along with glucose, it needs to be fermented to make the biomass-to-ethanol process economical. A lot of attention therefore has been focussed on the utilization of both glucose and xylose to ethanol. Accordingly, while describing the advancements that have taken place to get xylose converted efficiently to ethanol by xylose-fermenting organisms, the review deals mainly with the strategies that have been put forward for bioconversion of both the sugars to achieve high ethanol concentration, yield, and productivity. The approaches, which include the use of (1) xylose-fermenting yeasts alone, (2) xylose isomerase enzyme as well as yeast, (3) immobilized enzymes and cells, and (4) sequential fermentation and co-culture process are described with respect to their underlying concepts and major limitations. Genetic improvements in the cultures have been made either to enlarge the range of substrate utilization or to channel metabolic intermediates specifically toward ethanol. These contributions represent real significant advancements in the field and have also been adequately dealt with from the point of view of their impact on utilization of both cellulose and hemicellulose sugars to ethanol.     

Metabolic engineering applications to renewable resource utilization

Lignocellulosic materials containing cellulose, hemicellulose, and lignin are the most abundant renewable organic resource on earth. The utilization of renewable resources for energy and chemicals is expected to increase in the near future. The conversion of both cellulose (glucose) and hemicellulose (hexose and pentose) for the production of fuel ethanol is being studied intensively, with a view to developing a technically and economically viable bioprocess. Whereas the fermentation of glucose can be carried out efficiently, the bioconversion of the pentose fraction (xylose and arabinose, the main pentose sugars obtained on hydrolysis of hemicellulose), presents a challenge. A lot of attention has therefore been focused on genetically engineering strains that can efficiently utilize both glucose and pentoses, and convert them to useful compounds, such as ethanol. Metabolic strategies seek to generate efficient biocatalysts (bacteria and yeast) for the bioconversion of most hemicellulosic sugars to products that can be derived from the primary metabolism, such as ethanol. The metabolic engineering objectives so far have focused on higher yields, productivities and expanding the substrate and product spectra.     

The bioconversion of mountain pine beetle-killed lodgepole pine to fuel ethanol using the organosolv process

Lodgepole pine (Pinus contorta) killed by mountain pine beetle (Dendroctonus ponderosae) (BLP) was compared with healthy lodgepole pine (HLP) for bioconversion to ethanol and high-value co-products. The BLP and HLP chips were pretreated using an ethanol organosolv process at a variety of severities. It was shown that the BLP was easier to pretreat and delignify than were the HLP chips. The resulting pretreated BLP substrate had a lower residual lignin, lower degree of polymerization of cellulose, lower cellulose crystallinity, smaller fiber size and thereby a better enzymatic hydrolysability than did the HLP substrates. However, under the same conditions, the BLP showed lower substrate yield and cellulose recovery than did the HLP, which likely resulted from the excessive hydrolysis and subsequent decomposition of the cellulose and hemicellulose during the pretreatment. The BLP wood yielded more ethanol organosolv lignin than was obtained with the HLP material. The HLP lignin had a lower molecular weight and narrower distribution than did the BLP lignin. It appears that the beetle killed LP is more receptive to organosolv pretreatment other than a slightly lower recovery of carbohydrates.     

Characteristics of Corn Stover Pretreated with Liquid Hot Water and Fed-Batch Semi-Simultaneous Saccharification and Fermentation for Bioethanol Production

Corn stover is a promising feedstock for bioethanol production because of its abundant availability in China. To obtain higher ethanol concentration and higher ethanol yield, liquid hot water (LHW) pretreatment and fed-batch semi-simultaneous saccharification and fermentation (S-SSF) were used to enhance the enzymatic digestibility of corn stover and improve bioconversion of cellulose to ethanol. The results show that solid residues from LHW pretreatment of corn stover can be effectively converted into ethanol at severity factors ranging from 3.95 to 4.54, and the highest amount of xylan removed was approximately 89%. The ethanol concentrations of 38.4 g/L and 39.4 g/L as well as ethanol yields of 78.6% and 79.7% at severity factors of 3.95 and 4.54, respectively, were obtained by fed-batch S-SSF in an optimum conditions (initial substrate consistency of 10%, and 6.1% solid residues added into system at the prehydrolysis time of 6 h). The changes in surface morphological structure, specific surface area, pore volume and diameter of corn stover subjected to LHW process were also analyzed for interpreting the possible improvement mechanism.     

On the mechanism of direct conversion of cellulose to ethanol by Fusarium oxysporum: effect of cellulase and β-glucosidase

Summary The effects of the three main enzymes involved in cellulose saccharification, namely cellobiohydrolase, carboxymethylcellulase and -glucosidase, on the direct conversion of cellulose to ethanol by Fusarium oxysporum F3 were investigated. Ethanol production was not affected when the activity of the former two enzymes was varied within a wide range. By contrast, -glucosidase markedly affected ethanol production showing an optimum level of 0.7–0.8 unit/ml growth medium. A significant decrease of cellulose bioconversion time to ethanol was obtained when -glucosidase activity was adjusted to this optimal level at the beginning of the fermentation process. Offprint requests to: B. J. Macris