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。     

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。     

木薯纤维素乙醇发酵的纤维素酶成本评价

木薯中的纤维素成分约占木薯干重的10％(W/W).文中以木薯燃料乙醇生产的木薯纤维素酒渣为原料,从纤维素酶成本角度评估了三种利用木薯纤维素组分发酵生产乙醇的方法,包括木薯纤维素酒渣的直接糖化和乙醇发酵、木薯纤维素酒渣预处理后的糖化与乙醇发酵、木薯乙醇发酵中同步淀粉与纤维素糖化以及乙醇发酵.结果表明,前两种方法的纤维素利用效率不高,酶成本分别达到13602、11659元/吨乙醇.第三种方法,即在木薯乙醇发酵过程同时加入糖化酶和纤维素酶,进行同步淀粉与纤维素糖化,进而进行乙醇发酵,木薯纤维素乙醇的收益最高.发酵结束时的乙醇浓度从101.5g/L提高到107.0g/L,纤维素酶成本为3 589元/吨乙醇.此方法利用木薯纤维素与木薯淀粉同时进行,不会带来额外的设备及操作投入,酶成本低于产品乙醇价格,可实现盈利,因此第三种方法为木薯纤维用于乙醇发酵的最适方法,本研究结果将为木薯乙醇产业深度利用木薯纤维提供依据.     

一株葡萄糖和木糖共发酵高效产乙醇重组运动发酵单胞菌的性能评价

木糖是木质纤维素原料水解液中的第二大组分,木糖和葡萄糖的充分利用是有经济性地生产纤维素乙醇的关键。通过基因克隆手段构建了一株可以高效利用木糖产乙醇的重组运动发酵单胞菌Zymomonas mobilis TSH01,并进行了利用单糖溶液、混合糖溶液及玉米秸秆水解液发酵产乙醇效率的研究。结果表明,利用单一葡萄糖或单一木糖溶液发酵时,当糖浓度为8%、发酵72 h后,糖利用率分别为100%和98.9%,乙醇代谢收率分别为87.8%和78.3%;利用8%葡萄糖和8%木糖的混合溶液发酵时,72 h后,葡萄糖和木糖的利用率分别为98.5%和97.4%,乙醇代谢收率为94.9%。利用含3.2%葡萄糖和3.5%木糖的玉米秸秆水解液发酵72 h后,葡萄糖和木糖的利用率分别为100%和92.3%,乙醇代谢收率为91.5%。此外,磷酸二氢钾对发酵过程中木糖利用率以及乙醇收率的提高有明显促进作用。     

巢湖蓝藻与农业废弃物共热解制取生物质油研究

采用蔗渣、玉米秸秆和棉花秸秆3种废弃物与蓝藻进行混合共热解试验,考察废弃物的加入对蓝藻热解液体产率及组分的影响。结果表明:添加3种废弃物均使共热解液体产率呈下降趋势。当蓝藻与废弃物以1∶1混合共热解时,以蓝藻和玉米秸秆共热解液体产率最高,为61.8%,且除苯酚类以外,液体产物组分与单一蓝藻热解产物组分相近,含氮化合物含量明显降低,相对含量由18.49%降至8.15%。与其它2种废弃物相比,蓝藻与玉米秸秆在适当比例下的共热解有利于改善热解油品质。     

生物法脱除木质纤维素水解液中抑制因子的最新研究进展

实现从木质纤维素原料到燃料和高附加值化学品的生物转化,预处理是一个非常重要的步骤.酸解或蒸汽爆破等热-化学预处理过程会在水解液中生成或释放有机酸类、糠醛类和酚类化合物等抑制因子.这些抑制因子对发酵微生物具有毒性,会显著降低发酵产品的产率和生产强度.生物法去除木质纤维素水解液中的抑制因子具有操作简便以及不产生废水、废物等优点.生物脱毒法可分为两类:一类是通过向木质纤维素水解液中添加微生物或酶制剂,在发酵前去除抑制因子;另一类方法是通过遗传改造或适应性进化提高发酵菌株对抑制因子的生物降解能力,从而提高木质纤维素水解液的发酵性能.将着重以乙醇生产为例,介绍如何通过生物脱毒的方法提高木质纤维素水解液发酵的得率和生产强度.     

纤维素乙醇的生物炼制及研究进展

纤维素乙醇是以农业废弃生物质中的纤维素为主要原料、通过微生物发酵转化而成的生物燃料产品。作为一种绿色可再生替代能源,纤维素乙醇具有显著的能量收益和碳减排效益,对保障我国可持续发展、能源安全以及环境友好意义重大。然而,纤维素乙醇的生物炼制过程面临着难点和挑战。本文围绕纤维素原料及其预处理、纤维素酶水解和纤维素乙醇发酵工艺3个方面,介绍纤维素乙醇生物炼制的工艺流程及特征,剖析纤维素乙醇生产的主要技术瓶颈,并基于菌株抑制物胁迫耐性、碳源利用以及乙醇合成强化3个方面,总结了近年来纤维素乙醇生物炼制的研究进展,最后对纤维素乙醇未来的研究重点和发展前景进行了展望。     

纤维素乙醇高温发酵的研究进展与展望

利用高温细菌发酵,纤维素乙醇生产有望实现“生物质降解-乙醇发酵-乙醇蒸馏”过程的同步化,从而最大限度地降低纤维素乙醇的生产成本;这是一个目标更高、道路更远、科学性更强的可再生能源发展策略.纤维素乙醇高温发酵研究已经取得了重要进展,目前面临的主要挑战包括发酵乙醇的高温细菌的遗传转化系统不够稳定、缺少内源的高活性和耐热性纤维素酶,以及乙醇代谢调控机理有待进一步解析.这些科技难题将会在DNA生物合成和进化技术、细胞生物学技术,以及合成生物学技术的发展中得到解决.     

牛粪堆肥中纤维素高效降解菌的筛选与产酶条件优化

【背景】纤维素是一种有待开发利用的生物质资源,对于能源危机、环境污染问题的解决具有重要作用。【目的】从牛粪堆肥中分离出产纤维素酶的细菌,研究该菌株的纤维素降解能力。【方法】采用纤维素固体平板刚果红染色法进行初筛、液体发酵纤维素酶活测定法进行复筛。【结果】筛选获得一株具有高产纤维素酶活性的解淀粉芽孢杆菌(Bacillusamyloliquefaciens),命名为N5。单因素分析试验结果显示,菌株N5具有较好的pH、温度和盐度耐受性,正交优化试验结果表明,菌株N5产纤维素酶的最佳条件为：发酵初始pH 5.0,发酵时间96 h,发酵温度40℃。在此条件下,羧甲基纤维素(carboxymethyl cellulose, CMC)酶活为189.27 U/mL。此外,菌株N5能够在7 d内使水稻秸秆减重率达到19.35%。扫描电镜结果表明菌株N5能够有效促进水稻秸秆降解。【结论】菌株N5具有较高的纤维素酶活力,具有开发成高效好氧堆肥菌剂的潜质,这为固体废弃物中纤维素的生物转化提供了优质菌种资源。     

一种经济高效温和的生物质预处理新方法--动态挤压法

目前阻碍木质纤维原料生化转化为能源、材料或高附加值化学品的关键瓶颈问题是缺乏经济高效的生物质预处理及组分分离技术.本研究利用自行设计的动态挤压设备协同廉价化学药剂共作用处理玉米秸秆,通过挤压机对秸秆纤维的剪切、撕裂作用及化学脱木质素行为,解决传统单一物理或化学预处理方法能耗高、效率低及组分分离困难等问题,提高了纤维质生物转化的活性,降低预处理及组分分离过程的成本.与传统预处理工艺相比,整个过程用水量少、条件温和、能耗低,对后续生物转化过程有抑制作用的副产物生成量少,设备简单、易维护、易放大,具有良好的工业化前景.     

The enzymatic hydrolysis and fermentation of pretreated wheat straw to ethanol

Autohydrolysis and ethanol-alkali pulping were used as pretreatment methods of wheat straw for its subsequent saccharification by Trichoderma reesei cellulase. The basic hydrolysis parameters, i.e., reaction time, pH, temperature, and enzyme and substrate concentration, were optimized to maximize sugar yields from ethanol-alkali modified straw. Thus, a 93% conversion of 2.5% straw material to sugar syrup containing 73% glucose was reached in 48 h using 40 filter paper units/g hydrolyzed substrate. The pretreated wheat straw was then fermented to ethanol at 43 degrees C in the simultaneous saccharification and fermentation (SSF) process using T. reesei cellulase and Kluyveromyces fragilis cells. From 10% (w/v) of chemically treated straw (dry matter), 2.4% (w/v) ethanol was obtained after 48 h. When the T. reesei cellulase system was supplemented with beta-glucosidase from Aspergillus niger, the ethanol yield in the SSF process increased to 3% (w/v) and the reaction time was shortened to 24 h.     

Fast Pyrolysis of Biomass Residues in a Twin-screw Mixing Reactor

Fast pyrolysis is being increasingly applied in commercial plants worldwide. They run exclusively on woody biomass, which has favorable properties for conversion with fast pyrolysis. In order to increase the synergies of food production and the energetic and/or material use of biomass, it is desirable to utilize residues from agricultural production, e.g., straw. The presented method is suitable for converting such a material on an industrial scale. The main features are presented and an example of mass balances from the conversion of several biomass residues is given. After conversion, fractionated condensation is applied in order to retrieve two condensates — an organic-rich and an aqueous-rich one. This design prevents the production of fast pyrolysis bio-oil that exhibits phase separation. A two phase bio-oil is to be expected because of the typically high ash content of straw biomass, which promotes the production of water of reaction during conversion.Both fractionated condensation and the use of biomass with high ash content demand a careful approach for establishing balances. Not all kind of balances are both meaningful and comparable to other results from the literature. Different balancing methods are presented, and the information that can be derived from them is discussed.     

Enzymatische Hydrolyse und Ethanolgärung von Lignocellulosen

The kinetics of enzymatic hydrolysis of different lignocellulosic materials (wheat straw, newspaper and microcrystalline cellulose Avicel PH 101) was studied using the cellulase complexes from Trichoderma reesei QM 9414 and its mutants M 5, M 6, MHC 15 and MHC 22. The maximum yields of hydrolysis were obtained with wheat straw partially delignified with 1% NaOH as substrate, and using the enzyme from the mutants T. reesei M 6 and MHC 22. The possibility of simultaneous enzymatic hydrolysis and ethanol fermentation of wheat straw using the enzyme complex from M 6 and yeasts of the genus Candida and Torulopsis was also investigated. A good conversion of liberated glucose and cellobiose to ethanol was obtained, however, xylose was not fermented.     

湿氧化爆破稻秆的同步糖化发酵条件研究

探讨了木质纤维素经过湿氧化爆破后在同步糖化发酵过程中酵母产乙醇的基本规律.采用单因素方法对湿氧化爆破条件、酶系组成和添加量以及预酶解时间和温度进行了优化.不同湿氧化爆破预处理条件下的稻秆对同步糖化发酵工艺的影响较大,在预处理温度160 ℃,进氧压力为4×105 Pa,碱用量为6%(w/w),反应时间为20 min的条件...     

Dry biorefining maximizes the potentials of simultaneous saccharification and co‐fermentation for cellulosic ethanol production

Despite the well‐recognized merits of simultaneous saccharification and co‐fermentation (SSCF) on relieving sugar product inhibition on cellulase activity, a practical concomitance difficulty of xylose with inhibitors in the pretreated lignocellulose feedstock prohibits the essential application of SSCF for cellulosic ethanol fermentation. To maximize the SSCF potentials for cellulosic ethanol production, a dry biorefining approach was proposed starting from dry acid pretreatment, disk milling, and biodetoxification of lignocellulose feedstock. The successful SSCF of the inhibitor free and xylose conserved lignocellulose feedstock after dry biorefining reached a record high ethanol titer at moderate cellulase usage and minimum wastewater generation. For wheat straw, 101.4 g/L of ethanol (equivalent to 12.8% in volumetric percentage) was produced with the overall yield of 74.8% from cellulose and xylose, in which the xylose conversion was 73.9%, at the moderate cellulase usage of 15 mg protein per gram cellulose. For corn stover, 85.1 g/L of ethanol (equivalent to 10.8% in volumetric percentage) is produced with the overall conversion of 84.7% from cellulose and xylose, in which the xylose conversion was 87.7%, at the minimum cellulase usage of 10 mg protein per gram cellulose. Most significantly, the SSCF operation achieved the high conversion efficiency by generating the minimum amount of wastewater. Both the fermentation efficiency and the wastewater generation in the current dry biorefining for cellulosic ethanol production are very close to that of corn ethanol production, indicating that the technical gap between cellulosic ethanol and corn ethanol has been gradually filled by the advancing biorefining technology.     

Improving the remaining activity of lignocellulolytic enzymes by membrane entrapment

The production of bioethanol by the conversion of lignocellulosic waste has attracted much interest in recent years because of its low cost and great potential availability. However, the high cost of the enzyme required for this conversion is often considered to be the major bottleneck in the commercial lignocellulosic ethanol industry. In this work, the hydrolysis of rice straw by free and entrapped lignocellulolytic enzymes (cellulase, xylanase and laccase) was carried out at pH 5.5 and 37 °C. The hydrolysis of rice straw by enzymes entrapped in a membrane produced a higher monosaccharide content: 601.05 mg/g rice straw for entrapped enzymes vs. 465.46 mg/g rice straw for free enzymes. This study has shown that enzyme entrapment is an important technique for the efficient use and reuse of enzymes in industrial applications and also for the rapid separation of saccharide products from the reaction medium, thus improving the remaining enzymatic activities.     

Fractionation of wheat and barley straw to access high-molecular-mass hemicelluloses prior to ethanol production

The cost efficiency of the biorefining process can be improved by extracting high-molecular-mass hemicelluloses from lignocellulosic biomass prior to ethanol production. These hemicelluloses can be used in several high-value-added applications and are likely to be important raw materials in the future. In this study, steam pretreatment in an alkaline environment was used to pretreat the lignocellulosic biomass for ethanol production and, at the same time, extract arabinoxylan with a high-molecular-mass. It was shown that 30% of the arabinoxylan in barley straw could be extracted with high-molecular-mass, without dissolving the cellulose. The cellulose in the solid fraction could then be hydrolysed with cellulase enzymes giving a cellulose conversion of about 80–90% after 72 h. For wheat straw, more than 40% of the arabinoxylan could be extracted with high-molecular-mass and the cellulose conversion of the solid residue after 72 h was about 70–85%. The high cellulose conversion of the pretreated wheat and barley straw shows that they can be used for ethanol production without further treatment. It is therefore concluded that it is possible to extract high-molecular-mass arabinoxylan simultaneously with the pretreatment of biomass for ethanol production in a single steam pretreatment step.     

Thermal decomposition kinetics of wheat straw treated by Phanerochaete chrysosporium

Combining biological pretreatment with thermal processing may offer an alternative strategy for efficient conversion of lignocellulosic biomass into fuels and chemicals. The thermal decomposition kinetics of biologically pretreated wheat straw by Phanerochaete chrysosporium was investigated in this study using thermogravimetry (TG) - deconvoluted thermogravimetry (DTG) techniques and the Friedman method. This study revealed that biological pretreatment reduced the thermal degradation temperature of the biomass significantly. Relying on the thermal behavior of the biologically pretreated wheat straw, we proposed two biomass degradation phases during the biological degradation of wheat straw. The first phase of biodegradation (within 10 days of biological pretreatment) improved the efficiency of pyrolysis by reducing the temperature demand. In the second phase (after 10 days), although the efficiency of pyrolysis displayed the similar trend as the first phase, it showed a significant increase in activation energy demand. This process is greatly influenced by the residual lignin and cellulose ratios in the biomass. These experimental results will be useful in developing a biological pretreatment based thermochemical conversion process for lignocellulosic biomass.     

Hydrolysis of wheat straw hemicellulose with trifluoroacetic acid. Fermentation of xylose with Pachysolen tannophilus

Treatment of wheat straw with 1N trifluoroacetic acid (TFA) for 7 h at reflux temperature yielded 23% xylose based upon initial straw weight. This corresponds to about an 80% xylose yield based on the xylan content of the hemicellulose. The cellulose component of wheat straw was largely unaffected, as evidenced by low glucose yields. Decomposition of xylose by prolonged refluxing (23 h) was minimal in 1N TFA compared to 1N HCl. Treatment of wheat straw with refluxing 1N TFA converts about 10% of the lignin initially present in straw into water-soluble lignin fragments. Fermentation of the xylose-rich wheat straw hydrolyzate to ethanol with Pachysolen tannophilus was comparable to the fermentation of reagent grade xylose, indicating that furfural and toxic lignin by-products were not produced by 1N TFA in sufficient amounts to impair cell growth and ethanol production. Cellulase treatment of the wheat straw residue after TFA hydrolysis resulted in a 70-75% conversion of the cellulose into glucose.     

A UV-induced mutant of Pichia stipitis with increased ethanol production from xylose and selection of a spontaneous mutant with increased ethanol tolerance

In the fermentation process of lignocellulosic biomass (such as wood and rice straw), efficient conversion of pentose (mainly xylose) into ethanol is important. Mutants of Pichia stipitis NBRC1687 were obtained after UV mutagenesis and selection of large colonies on ethanol-containing medium. One mutant, PXF58, produced 4.3% ethanol from 11.4% xylose while the parent strain only produced 3.1%. The ethanol productivities of PXF58 from glucose and fructose were about were about 1.4-fold higher than those of the parent strain. After continuous cultivation of PXF58 in YNB (yeast nitrogen base) medium containing 2% xylose and 5-7% ethanol, an ethanol-tolerant mutant, PET41, was obtained. Strain PET41 was able to produce 4.4% ethanol when first supplied with xylose then with glucose. This isolate might be thus useful for two-phase fermentation in which xylan is saccharified by xylanase to produce xylose, and glucan is saccharified later by cellulase and β-glucosidase to produce glucose.