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Optimal control of dilute acid pretreatment and enzymatic hydrolysis for processing lignocellulosic feedstock

机译:稀酸预处理和加工木质纤维素原料的酶促水解的最佳控制

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Lignocellulosic feedstock is one of the potential renewable sources for producing ethanol for transportation. The process steps viz., acid pretreatment and enzymatic hydrolysis in bio-chemical process route are intended to produce fermentable sugars, which can be readily fermented for producing ethanol. However, the dilute acid pre-treatment and enzymatic hydrolysis process steps are found to be economically inefficient. The present work aims at optimizing these process steps for improving the process performance. Such optimization is expected to increase conversion, reduce energy or material requirement, thereby improving the economics. The kinetic models of acid pretreatment and enzymatic hydrolysis for lignocellulosic feedstock processing are adapted from literature. Subsequently, these kinetic models are augmented by associated mass and energy balances, to develop a batch reactor model and fed-batch reactor model for dilute acid pretreatment and enzymatic hydrolysis processes, respectively. Optimal control with Pontryagin's maximum principle has been implemented to determine the optimal time dependent profiles of heating and cooling fluid flow rates and operating temperatures for acid pretreatment and substrate feed rate profile for enzymatic hydrolysis to optimize the respective processes performance. Different objective functions such as maximizing concentration of desired product, minimizing the batch time, and maximizing profit have been considered. The simulation results yielded an increase of 6.7% and 8.8% in final concentration of desired product; 43% and 42.5% reduction in batch processing time for pretreatment and enzymatic hydrolysis processes, respectively. Finally, the simulation results have also provided optimal operating policies which have increased the profit of pretreatment by 124% and enzymatic hydrolysis by 150%, thereby improving the techno-economic feasibility for processing lignocellulosic feedstock. (C) 2017 Elsevier Ltd. All rights reserved.
机译:木质纤维素原料是用于生产乙醇的潜在可再生能源之一。该方法步骤Ziz,生物化学过程途径中的酸预处理和酶水解旨在产生可发酵的糖,可以易于发酵生产乙醇。然而,发现稀酸预处理和酶水解过程步骤在经济上是低效率的。本工作旨在优化这些过程步骤,以提高过程性能。这种优化预计会增加转换,降低能量或材料要求,从而改善经济学。用于木质纤维素原料加工的酸预处理和酶水解的动力学模型适用于文献。随后,这些动力学模型通过相关的质量和能量余额增强,分别为稀酸预处理和酶水解方法开发批量反应器模型和补料批量反应器模型。已经实施了利用Pontryagin的最大原理的最佳控制,以确定加热和冷却流体流速的最佳时间依赖性曲线以及酸预处理的操作温度和用于酶水解的基板进料速率曲线,以优化各自的过程性能。考虑了不同的目标功能,例如最大化所需产品的浓度,最小化批量时间,并最大限度地提高利润。所需产品的最终浓度的仿真结果产生了6.7%和8.8%;分批加工时间减少43%和42.5%,用于预处理和酶水解过程。最后,仿真结果还提供了最佳的操作策略,这些策略将预处理的利润增加了124%和酶水解150%,从而提高了加工木质纤维素原料的技术经济可行性。 (c)2017 Elsevier Ltd.保留所有权利。

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