酵母发酵蔗渣半纤维素水解物生产木糖酶

采用二次正交旋转组合设计研究了蔗渣半纤维素水解过程中硫酸浓度与液 固比对木糖收率的影响。回归分析表明 ,这两个因素与木糖的收率之间存在显著的回归关系。通过回归方程优化水解条件 ,当硫酸浓度 2 .4g L ,液 固 =6 .2 ,在蒸汽压力 2 .5× 10 4Pa的条件下水解 2 .5h ,10 0g蔗渣可水解生成木糖约 2 4g。大孔树脂吸附层析处理蔗渣半纤维素水解物 ,能有效地减少其中的酵母生长抑制物含量 ,显著改善水解物的发酵性能。用大孔树脂在pH 2条件下处理过的蔗渣半纤维素水解物作基质 ,含木糖 2 0 0g L ,产木糖醇酵母菌株CandidatropicalisAS2 .1776发酵 110h耗完基质中的木糖 ,生成木糖醇 12 7g L ,产物转化率 0 .6 4(木糖醇g 木糖g) ,产物生成速率 1.15g L·h .     

Simultaneous saccharification and fermentation of steam-pretreated bagasse using Saccharomyces cerevisiae TMB3400 and Pichia stipitis CBS6054

Sugarcane bagasse--a residue from sugar and ethanol production from sugar cane--is a potential raw material for lignocellulosic ethanol production. This material is high in xylan content. A prerequisite for bioethanol production from bagasse is therefore that xylose is efficiently fermented to ethanol. In the current study, ethanolic fermentation of steam-pretreated sugarcane bagasse was assessed in a simultaneous saccharification and fermentation (SSF) set-up using either Saccharomyces cerevisiae TMB3400, a recombinant xylose utilizing yeast strain, or Pichia stipitis CBS6054, a naturally xylose utilizing yeast strain. Commercial cellulolytic enzymes were used and the content of water insoluble solids (WIS) was 5% or 7.5%. S. cerevisiae TMB3400 consumed all glucose and large fraction of the xylose in SSF. Almost complete xylose conversion could be achieved at 5% WIS and 32 degrees C. Fermentation did not occur with P. stipitis CBS6054 at pH 5.0. However, at pH 6.0, complete glucose conversion and high xylose conversion (>70%) was obtained. Microaeration was required for P. stipitis CBS6054. This was not necessary for S. cerevisiae TMB3400.     

Production of cellulases and hemicellulases by Penicillium echinulatum grown on pretreated sugar cane bagasse and wheat bran in solid-state fermentation

AIM: To evaluate the solid-state fermentation (SSF) production of cellulase and hemicellulases (xylanases), by Penicillium echinulatum 9A02S1, in experiments carried out with different concentrations of the pretreated sugar cane bagasse (PSCB) and wheat bran (WB). METHODS AND RESULTS: This study reports the production of xylanolytic and cellulolytic enzymes by P. echinulatum 9A02S1 using a cheap medium containing PSCB and WB under SSF. The highest amounts of filter paper activity (FPA) could be measured on mixtures of PSCB and WB (32.89 +/- 1.90 U gdm(-1)). The highest beta-glucosidase activity was 58.95 +/- 2.58 U gdm(-1) on the fourth day. The highest activity for endoglucanases was 282.36 +/- 1.23 U gdm(-1) on the fourth day, and for xylanases the activity was around 10 U gdm(-1) from the second to the fourth day. CONCLUSIONS: The present work has established the potential of P. echinulatum for FPA, endoglucanase, beta-glucosidase and xylanase productions in SSF, indicating that WB may be partially substituted by PSCB. SIGNIFICANCE AND IMPACT OF THE STUDY: The incorporation of cheap sources, such as sugar cane bagasse, into media for the production of lignocellulose enzymes should help decrease the production costs of enzymatic complexes that can hydrolyse lignocellulose residues for the formation of fermented syrups, thus contributing to the economic production of bioethanol.     

Production of lipases by solid state fermentation using vegetable oil-refining wastes

Lipases were produced by a microbial consortium derived from a mixture of wastewater sludges in a medium containing solid industrial wastes rich in fats, under thermophilic conditions (temperature higher than 45 °C for 20 days) in 4.5-L reactors. The lipases were extracted from the solid medium using 100 mM Tris–HCl, pH 8.0 and a cationic surfactant agent (cetyltrimethylammonium chloride). Different doses of surfactant and buffer were tested according to a full factorial experimental design. The extracted lipases were most active at 61–65 °C and at pH 7.7–9. For the solid samples, the lipolytic activity reached up to 120,000 UA/g of dry matter. These values are considerably higher than those previously reported in literature for solid-state fermentation and highlight the possibility to work with the solid wastes as effective biocatalysts.     

Exploitation of biological wastes for the production of value-added products under solid-state fermentation conditions

Biological wastes contain several reusable substances of high value such as soluble sugars and fibre. Direct disposal of such wastes to soil or landfill causes serious environmental problems. Thus, the development of potential value-added processes for these wastes is highly attractive. These biological wastes can be used as support-substrates in solid-state fermentation (SSF) to produce industrially relevant metabolites with great economical advantage. In addition, it is an environmentally friendly method of waste management. This paper reviews the reutilization of biological wastes for the production of value-added products using the SSF technique.     

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.     

氨水湿磨对稻草厌氧发酵的促进作用

提出了为改善稻草厌氧发酵效率的氨水湿磨预处理方法.首先对稻草进行剪切、粗粉碎和氨水湿磨处理,然后采用单相法对预处理稻草进行厌氧发酵,以把握稻草厌氧发酵中反应速率和发酵料液pH的变化特征,探明材料大小、氨水质量分数对稻草厌氧发酵反应速率和产气率的影响.结果表明:稻草厌氧发酵可分为初期、中期和后期3个阶段.发酵料液pH在发酵初期呈下降趋势,在发酵中期和后期基本稳定在6.5～7.0.氨水湿磨处理不仅减小了稻草的材料尺寸,而且能松弛组织结构、提高碳氮比.采用质量分数为0.2%的氨水对稻草进行湿磨处理后,平均产气速率和产气率分别从剪切稻草的7mL/(g·d)、216mL/g增加到14mL/(g·d)、378mL/g.     

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.     

Identification of Dekkera bruxellensis as a major contaminant yeast in continuous fuel ethanol fermentation

AIMS: To identify and characterize the main contaminant yeast species detected in fuel-ethanol production plants in Northeast region of Brazil by using molecular methods. METHODS AND RESULTS: Total DNA from yeast colonies isolated from the fermentation must of industrial alcohol plants was submitted to PCR fingerprinting, D1/D2 28S rDNA sequencing and species-specific PCR analysis. The most frequent non-Saccharomyces cerevisiae isolates were identified as belonging to the species Dekkera bruxellensis, and several genetic strains could be discriminated among the isolates. The yeast population dynamics was followed on a daily basis during a whole crop harvesting period in a particular industry, showing the potential of D. bruxellensis to grow faster than S. cerevisiae in industrial conditions, causing recurrent and severe contamination episodes. CONCLUSIONS: The results showed that D. bruxellensis is one of the most important contaminant yeasts in distilleries producing fuel-ethanol from crude sugar cane juice, specially in continuous fermentation systems. SIGNIFICANCE AND IMPACT OF THE STUDY: Severe contamination of the industrial fermentation process by Dekkera yeasts has a negative impact on ethanol yield and productivity. Therefore, early detection of D. bruxellensis in industrial musts may avoid operational problems in alcohol-producing plants.     

Enzymatic saccharification of sugar cane bagasse by continuous xylanase and cellulase production from cellulomonas flavigena PR‐22

Cellulase (CMCase) and xylanase enzyme production and saccharification of sugar cane bagasse were coupled into two stages and named enzyme production and sugar cane bagasse saccharification. The performance of Cellulomonas flavigena (Cf) PR‐22 cultured in a bubble column reactor (BCR) was compared to that in a stirred tank reactor (STR). Cells cultured in the BCR presented higher yields and productivity of both CMCase and xylanase activities than those grown in the STR configuration. A continuous culture with Cf PR‐22 was run in the BCR using 1% alkali‐pretreated sugar cane bagasse and mineral media, at dilution rates ranging from 0.04 to 0.22 1/h. The highest enzymatic productivity values were found at 0.08 1/h with 1846.4 ± 126.4 and 101.6 ± 5.6 U/L·h for xylanase and CMCase, respectively. Effluent from the BCR in steady state was transferred to an enzymatic reactor operated in fed‐batch mode with an initial load of 75 g of pretreated sugar cane bagasse; saccharification was then performed in an STR at 55°C and 300 rpm for 90 h. The constant addition of fresh enzyme as well as the increase in time of contact with the substrate increased the total soluble sugar concentration 83% compared to the value obtained in a batch enzymatic reactor. This advantageous strategy may be used for industrial enzyme pretreatment and saccharification of lignocellulosic wastes to be used in bioethanol and chemicals production from lignocellulose. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:321–326, 2016     

碳氮比对模拟水稻秸秆田间厌氧发酵系统甲烷生产和秸秆降解的影响

利用自制的厌氧发酵装置模拟田间厌氧发酵产生物甲烷的条件,通过添加不同量的尿素,研究C/N对水稻秸秆厌氧发酵产生物甲烷和秸秆降解的影响。设置了C/N为15∶1、20∶1、25∶1、30∶1和对照(53∶1)等五个处理,测定各处理的产气量、甲烷含量和秸秆木质纤维素含量。结果表明C/N对厌氧发酵产气进程有一定影响,峰值出现的时间、峰值的大小在不同处理之间均有差异:以C/N为25∶1的处理峰值出现的最早,较对照早5 d出现;以C/N为20∶1的峰值最高,较对照提高了27. 55%。C/N对厌氧发酵累积产气量和累积甲烷产量有显著影响,以C/N为20∶1的处理累积产气量(4 235. 00 mL)和累积甲烷产量(1526. 34mL)最高,相比对照组的累积产气量和累积甲烷产量分别提高了30. 78%和51. 31%。C/N对水稻秸秆降解也有显著影响。以20∶1和25∶1处理对秸秆降解的效果最好,其中20∶1处理的总降解率、纤维素降解率和半纤维素降解率分别达到了51. 33%、55. 31%和53. 05%,25∶1处理分别为50. 00%、53. 08%和49. 42%。上述结果表明通过添加尿素调节C/N能够提高水稻秸秆厌氧发酵的产生物甲烷效率和促进秸秆降解,以C/N为(20～25)∶1处理的促进效果最好。     

不同预处理及发酵方式对提高蔗渣发酵产物蛋白含量的研究

采用不同的预处理方法对蔗渣进行预处理,并测定了其各个组分的含量。利用霉菌对蔗渣进行微生物降解,并讨论了不同发酵方式对产物中蛋白含量的影响。结果表明,木霉与热带假丝酵母共发酵时蛋白含量最高,为17．74％。     

绿色木霉ZY-1固态发酵产纤维素酶

利用筛选的绿色木霉ZY-1（Trichoderma viride ZY-1）固态发酵产纤维素酶,采用稻草和麸皮为底物,考察稻草与麸皮比例随发酵时间对产酶的影响。结果表明：底物中,在m（稻草）：m（麸皮）为0：5和1：4时,发酵48h,pH保持4．5左右,还原糖量急剧上升,胞外蛋白产量最低;仅以稻草作底物时,整个发酵过程中pH约为7,还原糖量最低,胞外蛋白产量较高而滤纸酶活、羧甲基纤维素酶（CMCase）和β-葡萄糖苷酶（β-Gase）酶活均较低;在m（稻草）：m（麸皮）为3：2时,发酵96h,滤纸酶活达最大值5．01U／g干曲;m（稻草）：m（麸皮）为1：4时,发酵96h,β-Gase酶活达最大值4．6U／g干曲;m（稻草）：m（麸皮）为4：1时,发酵72h,CMCase酶活达最大值6．01U／g干曲。因此,底物中存在适量的稻草和麸皮有利于Trichoderma viride ZY—1产纤维素酶。     

Enzymatic digestion of alkaline‐sulfite pretreated sugar cane bagasse and its correlation with the chemical and structural changes occurring during the pretreatment step

Sugar cane bagasse is recalcitrant to enzymatic digestion, which hinders the efficient conversion of its polysaccharides into fermentable sugars. Alkaline‐sulfite pretreatment was used to overcome the sugar cane bagasse recalcitrance. Chemical and structural changes that occurred during the pretreatment were correlated with the efficiency of the enzymatic digestion of the polysaccharides. The first 30 min of pretreatment, which removed approximately half of the initial lignin and 30% of hemicellulose seemed responsible for a significant enhancement of the cellulose conversion level, which reached 64%. After the first 30 min of pretreatment, delignification increased slightly, and hemicellulose removal was not enhanced; however, acid groups continued to be introduced into the residual lignin. Water retention values were 145% to the untreated bagasse and 210% to the bagasse pretreated for 120 min and fiber widths increased from 10.4 to 30 μm, respectively. These changes were responsible for an additional increase in the efficiency of enzymatic hydrolysis of the cellulose, which reached 92% with the 120 min pretreated sample. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:890–895, 2013     

Accumulation of recombinant cellobiohydrolase and endoglucanase in the leaves of mature transgenic sugar cane

A major strategic goal in making ethanol from lignocellulosic biomass a cost-competitive liquid transport fuel is to reduce the cost of production of cellulolytic enzymes that hydrolyse lignocellulosic substrates to fermentable sugars. Current production systems for these enzymes, namely microbes, are not economic. One way to substantially reduce production costs is to express cellulolytic enzymes in plants at levels that are high enough to hydrolyse lignocellulosic biomass. Sugar cane fibre (bagasse) is the most promising lignocellulosic feedstock for conversion to ethanol in the tropics and subtropics. Cellulolytic enzyme production in sugar cane will have a substantial impact on the economics of lignocellulosic ethanol production from bagasse. We therefore generated transgenic sugar cane accumulating three cellulolytic enzymes, fungal cellobiohydrolase I (CBH I), CBH II and bacterial endoglucanase (EG), in leaves using the maize PepC promoter as an alternative to maize Ubi1 for controlling transgene expression. Different subcellular targeting signals were shown to have a substantial impact on the accumulation of these enzymes; the CBHs and EG accumulated to higher levels when fused to a vacuolar-sorting determinant than to an endoplasmic reticulum-retention signal, while EG was produced in the largest amounts when fused to a chloroplast-targeting signal. These results are the first demonstration of the expression and accumulation of recombinant CBH I, CBH II and EG in sugar cane and represent a significant first step towards the optimization of cellulolytic enzyme expression in sugar cane for the economic production of lignocellulosic ethanol.     

木质纤维素原料酶水解产乙醇工艺的研究进展

木质纤维素原料预处理后,经水解、发酵等过程,可生产乙醇作为清洁燃料,这大大提高了农业和林业废弃物的利用率,减轻了环境污染,并为经济的可持续发展提供了保证。目前木质纤维素酶水解因其具有明显优势而受到重视,被普遍研究和采用。综述了近年来木质纤维素原料的预处理方法、酶与水解技术、发酵工艺以及发酵耦合分离技术的最新研究成果。     

A kinetic model for simultaneous saccharification and fermentation of Avicel with Saccharomyces cerevisiae

This work describes a numerical model for predicting simultaneous saccharification and fermentation of Avicel, an insoluble crystalline cellulose polymer. Separate anoxic cultivations of 40 g/L glucose and 100 g/L Avicel were conducted to verify model predictions and obtain parameters to describe the reaction kinetics. Saccharification of Avicel was achieved with Trichoderma reesei cellulases from the enzyme preparation Spezyme CP with an enzyme loading of 10 FPU/g cellulose. Cultivations were supplemented with 50 IU/g cellulose of β‐glucosidase from Novozym 188 to prevent product inhibition by cellobiose. Saccharomyces cerevisiae MH‐1000 is a robust industrial strain and was used to ferment glucose to ethanol, glycerol, and carbon dioxide. The numerical model presented in this paper differs from previous models by separating the endoglucanase and exoglucanase enzyme kinetics and allowing for inhibitive site competition. Assuming all enzymes remain active and that each enzyme complex has a corresponding constant specific activity, the model is capable of predicting adsorbed enzyme concentrations with reasonable accuracy. Comparison of predicted values to experimental measurements indicated that the numerical model was capable of capturing the significant elements involved with cellulose conversion to ethanol. Biotechnol. Bioeng. 2011; 108:924–933. © 2010 Wiley Periodicals, Inc.