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Biocatalysis and Biotransformation of Lignocellulose into Bioethanol: Process Intensification and Mechanism Research

机译:木素纤维素生物催化转化为生物乙醇的过程​​强化及机理研究

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As one kind of non-renewable resources, fossil fuels will be exhausted in the near future.At the constant production and consumption, the presently known reserves of oil will lastaround 45.7 years, natural gas 62.8 years, and coal 119 years(1). In addition, globalwarming caused by greenhouse gas emission attribute mostly to the combustion of fossilfuels. Bioethanol is one of the most potential renewable energies. For large-scale usage,lignocellulosic material is a promising choice to produce a second generation bioethanolfuel(2). As the renewable source, lignocellulose not only has extensive sources, such assugarcane bagasse, corn stover, corncob, wheat straw, sawdust, etc, but also significantlydecrease net the carbon dioxide emission. However, there are a number of obstacles suchas slow reaction rate, high production costs, non-cellulosic material block, and low ethanolconcentration, which diminishing the enzyme performance and hinder the progress ofbiomass industrialization(3,4). To decrease reducing product inhibition effect oncellobiohydrolases and β-glucosidase, simultaneous saccharification and fermentation(SSF) is often used in bio-ethanol production by fermentable sugars to ethanol timely(5). Atthe same time, various strategies were performed for the purpose of cost-effectiveenzymatic conversion such as reducing enzymes production cost, producing cellulase withhigher specific activity(6) and enzyme recycling including cellulase adsorption onto freshsubstrate(7) and cellulase immobilization(8,9).This paper summarizes our work on biocatalysis and biotransformation of lignocelluloseinto bioethanol aiming to enhance enzyamtic hydrolysis efficiency and increase final ethanolconcentration, and the mechanism of cellulase on cellulose was also investigated.(1) Enzyme complex. Hemicellulose and possibly pectin are thought to restrict theaccess of cellulases to their substrate in pretreated lignocellulose. Addition of xylanasesand pectinases can degrade these non-cellulosic saccharides and thus increase celluloseconversion(10). The digestion of cellulose was increased by enzyme complexes of cellulaseand accessory enzymes including β-glucosidase, xylanase and pectinase to hydrolyzecellobiose, hemicellulose and pectin, respectively (Fig. 1).To enhance the conversion of the cellulose and hemicellulose, the corncob pretreated byaqueous ammonia soaking was hydrolyzed by enzyme complexes. Firstly, corncob werepretreated by aqueous ammonia soaking and the saturation limits for cellulase and β-glucosidase were determined, which is 15mg protein/g glucan (50FPU/g glucan) forcellulase (Spezyme CP). Second, the accessory enzymes (β-glucosidase, xylanase andpectinase) were supplemented to hydrolyze cellobiose (cellulase-inhibiting product),hemicellulose and pectin (the component covering the fiber surfaces), respectively. It wasfound that β-glucosidase (Novozyme 188) loading of 1.45mg protein/g glucan (30CBU/g
机译:作为一种不可再生资源,化石燃料将在不久的将来耗尽。 在恒定的生产和消耗下,目前已知的石油储量将持续 大约45.7年,天然气62.8年,煤炭119年(1)。此外,全球 温室气体排放引起的变暖主要归因于化石的燃烧 燃料。生物乙醇是最有潜力的可再生能源之一。为了大规模使用, 木质纤维素材料是生产第二代生物乙醇的有前途的选择 燃料(2)。作为可再生资源,木质纤维素不仅具有广泛的来源,例如 甘蔗渣,玉米秸秆,玉米芯,麦秸,锯末等,但也明显 减少二氧化碳的净排放量。但是,存在许多障碍,例如 反应速度慢,生产成本高,非纤维素原料块,乙醇含量低 浓度,这会降低酶的性能并阻碍酶的进程 生物质工业化(3,4)。减少对产品的抑制作用 纤维二糖水解酶和β-葡萄糖苷酶,同时糖化和发酵 (SSF)通常用于将可发酵糖适时地转化为乙醇的生物乙醇生产(5)。在 同时,出于成本效益的目的执行了各种策略 酶促转化,例如降低酶的生产成本,生产纤维素酶 更高的比活性(6)和酶回收,包括纤维素酶吸附到新鲜的 底物(7)和纤维素酶固定化(8,9)。 本文总结了我们在木质纤维素的生物催化和生物转化方面的工作。 进入生物乙醇旨在提高酶水解效率并增加最终乙醇 还研究了纤维素酶的浓度,以及纤维素酶对纤维素的作用机理。 (1)酶复合物。半纤维素和可能的果胶被认为限制了 在预处理的木质纤维素中纤维素酶接近其底物的能力。木聚糖酶的添加 果胶酶可以降解这些非纤维素糖类,从而增加纤维素 conversion(10)。纤维素酶复合物增加了纤维素的消化 和辅助酶,包括β-葡萄糖苷酶,木聚糖酶和果胶酶水解 纤维二糖,半纤维素和果胶(图1)。 为了提高纤维素和半纤维素的转化率,对玉米芯进行了预处理 氨水浸泡被酶复合物水解。首先,玉米芯是 氨水浸泡预处理和纤维素酶和β-的饱和极限 测定的葡糖苷酶为15mg蛋白质/ g葡聚糖(50FPU / g葡聚糖) 纤维素酶(Spezyme CP)。其次,辅助酶(β-葡萄糖苷酶,木聚糖酶和 补充果胶酶以水解纤维二糖(纤维素酶抑制产物), 半纤维素和果胶(覆盖纤维表面的成分)。它是 发现β-葡萄糖苷酶(Novozyme 188)负载1.45mg蛋白质/ g葡聚糖(30CBU / g

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