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酶解木质纤维素过程中最小化产物抑制的反应器设计:II. 抑制的定量分析和膜反应器的适用性。

Reactor design for minimizing product inhibition during enzymatic lignocellulose hydrolysis: II. Quantification of inhibition and suitability of membrane reactors.

机构信息

Department of Chemical and Biochemical Engineering, Technical University of Denmark, DK-2800 Kgs. Lyngby, Denmark.

出版信息

Biotechnol Adv. 2010 May-Jun;28(3):407-25. doi: 10.1016/j.biotechadv.2010.02.005. Epub 2010 Feb 19.

Abstract

Product inhibition of cellulolytic enzymes affects the efficiency of the biocatalytic conversion of lignocellulosic biomass to ethanol and other valuable products. New strategies that focus on reactor designs encompassing product removal, notably glucose removal, during enzymatic cellulose conversion are required for alleviation of glucose product inhibition. Supported by numerous calculations this review assesses the quantitative aspects of glucose product inhibition on enzyme-catalyzed cellulose degradation rates. The significance of glucose product inhibition on dimensioning of different ideal reactor types, i.e. batch, continuous stirred, and plug-flow, is illustrated quantitatively by modeling different extents of cellulose conversion at different reaction conditions. The main operational challenges of membrane reactors for lignocellulose conversion are highlighted. Key membrane reactor features, including system set-up, dilution rate, glucose output profile, and the problem of cellobiose are examined to illustrate the quantitative significance of the glucose product inhibition and the total glucose concentration on the cellulolytic conversion rate. Comprehensive overviews of the available literature data for glucose removal by membranes and for cellulose enzyme stability in membrane reactors are given. The treatise clearly shows that membrane reactors allowing continuous, complete, glucose removal during enzymatic cellulose hydrolysis, can provide for both higher cellulose hydrolysis rates and higher enzyme usage efficiency (kg(product)/kg(enzyme)). Current membrane reactor designs are however not feasible for large scale operations. The report emphasizes that the industrial realization of cellulosic ethanol requires more focus on the operational feasibility within the different hydrolysis reactor designs, notably for membrane reactors, to achieve efficient enzyme-catalyzed cellulose degradation.

摘要

产物抑制纤维素酶会影响木质纤维素生物量转化为乙醇和其他有价值产品的生物催化效率。需要新的策略来关注反应器设计,包括在酶促纤维素转化过程中去除产物,特别是葡萄糖,以缓解葡萄糖产物抑制。本综述通过大量计算评估了葡萄糖产物抑制对酶催化纤维素降解速率的定量影响。通过对不同反应条件下不同纤维素转化率的建模,定量说明了葡萄糖产物抑制对不同理想反应器类型(如间歇式、连续搅拌式和推流式)设计的重要性。突出了膜反应器用于木质纤维素转化的主要操作挑战。重点考察了膜反应器的关键特征,包括系统设置、稀释率、葡萄糖输出曲线以及纤维二糖问题,以说明葡萄糖产物抑制和总葡萄糖浓度对纤维素转化率的定量意义。还对膜去除葡萄糖和膜反应器中纤维素酶稳定性的现有文献数据进行了全面综述。本文清楚地表明,允许在酶促纤维素水解过程中连续、完全去除葡萄糖的膜反应器,可以提供更高的纤维素水解速率和更高的酶使用效率(kg(产物)/kg(酶))。然而,目前的膜反应器设计不适用于大规模操作。该报告强调,纤维素乙醇的工业化实现需要更加关注不同水解反应器设计的操作可行性,特别是对于膜反应器,以实现有效的酶促纤维素降解。

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