Nagle Nicholas J, Elander Richard T, Newman Mildred M, Rohrback Brian T, Ruiz Raymond O, Torget Robert W
National Renewable Energy Laboratory, Biotechnology Division for Fuels and Chemicals, 1617 Cole Blvd., Golden, Colorado 80401, USA.
Biotechnol Prog. 2002 Jul-Aug;18(4):734-8. doi: 10.1021/bp0155078.
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
降低预处理和生物转化过程的成本是生物乙醇产业成功发展的关键目标。长期以来,这些单元操作因其对乙醇生产成本的影响而受到认可。实现这一目标的一种策略是改进预处理过程,以生产经过预处理的底物,从而缩短生物转化时间、降低纤维素酶用量和/或提高乙醇产量。先前的研究使用多阶段、连续流动、极稀硫酸(0.07%(w/v))预处理方法制备了一种高度可消化的预处理黄杨木底物。该过程减少了将预处理的黄杨木屑生物转化为乙醇所需的时间,从而显著提高了纤维素乙醇的产量。然而,该过程的液体体积需求、蒸汽需求以及流通式反应器配置的复杂性被认为是其商业化的严重障碍。已开发出一种重新配置的过程,通过单阶段间歇预处理,随后进行固液分离,并在130至150摄氏度之间的温度下洗涤固体,以实现类似的性能。据信,在高温下进行分离和洗涤可防止大部分溶解的木质素和木聚糖重新沉淀和/或与预处理后的固体重新结合。在高温下对固体进行洗涤,既提高了可溶性木糖的回收率,又使预处理后的底物更易于酶解。关键操作变量和过程性能指标包括酸浓度、温度、洗涤体积、洗涤温度、可溶性木糖回收率以及经过洗涤的预处理固体在同步糖化发酵(SSF)生物转化中的性能。初步结果表明,与对照(不洗涤、不分离)相比,热洗涤材料在72小时时的乙醇产量提高了50%以上,并且从纤维素获得高乙醇产量所需的生物转化时间减少了43%