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Efficacy of a hot washing process for pretreated yellow poplar to enhance bioethanol production

机译:预处理黄杨的热洗过程可提高生物乙醇的生产效率

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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 degreesC. 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.
机译:减少预处理和生物转化过程的成本是成功部署生物乙醇行业所必需的关键目标。这些单元操作对乙醇生产成本的影响早已得到认可。实现该目标的一种策略是改进预处理过程以生产预处理的底物,从而减少生物转化时间,降低纤维素酶的使用量和/或提高乙醇产量。先前的研究使用多阶段,连续流动,非常稀的硫酸(0.07%(w / v))预处理生产了高度易消化的预处理黄杨基质。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。这导致纤维素中乙醇的产率大大提高。然而,液体体积需求,蒸汽需求和流通式反应器配置的复杂性被确定为该方法商业化的严重障碍。已经开发出一种重新配置的工艺,以实现类似的性能,该工艺使用单阶段的间歇预处理,然后分离固体和液体,并在130至150摄氏度之间的温度下洗涤固体。据信在高温下的分离和洗涤可防止大部分的溶解的木质素和木聚糖与预处理的固体再沉淀和/或再结合。固体在高温下的这种洗涤导致较高的可溶性木糖糖回收率和更易消化的用于酶水解的预处理底物。关键的操作变量和过程性能指标包括酸浓度,温度,洗涤量,洗涤温度,可溶性木糖回收率以及经过洗涤,预处理的固体通过同时糖化和发酵(SSF)进行生物转化的性能。初步结果表明,与对照相比(不洗涤,不分离),热洗后的材料在72小时内乙醇收率提高了50%以上,从纤维素中获得高乙醇收率所需的生物转化时间减少了43%。

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