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首页> 外文期刊>Journal of Cleaner Production >Circulating fluidized bed gasification of biomass for flexible end-use of syngas: a micro and nano scale study for production of bio-methanol
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Circulating fluidized bed gasification of biomass for flexible end-use of syngas: a micro and nano scale study for production of bio-methanol

机译:生物质的循环流化床气化,用于灵活的合成气最终用途:用于生产生物甲醇的微米和纳米级研究

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摘要

Biomass gasification in circulating fluidized bed gasifiers (CFBGs) is regarded as one of the major options for clean heat and power generation, due to good gas-solid mixing. In this paper, we developed an Aspen Plus model to simulate the methanol production from biomass derived syngas by integrating the bed hydrodynamics and reaction kinetics. Particular emphasis placed on the influence of steam/biomass ratio (S/B), gasification temperature, equivalence ratio (ER), and biomass particle size (BPS) on methanol yield. The simulation results demonstrated that ER and gasification temperature are the most important factors in the process; higher ER and temperature contributed to lower and higher methanol yield, respectively. Model predictions were compared with available data from the literature, which showed fully good agreement (C) 2016 Elsevier Ltd. All rights reserved.
机译:由于良好的气固混合,循环流化床气化炉(CFBG)中的生物质气化被视为清洁热力和发电的主要选择之一。在本文中,我们开发了一个Aspen Plus模型,通过整合床的流体动力学和反应动力学来模拟由生物质衍生的合成气生产甲醇。特别强调蒸汽/生物质比(S / B),气化温度,当量比(ER)和生物质粒径(BPS)对甲醇收率的影响。仿真结果表明,ER和气化温度是该过程中最重要的因素。较高的ER和温度分别导致较低和较高的甲醇收率。将模型预测与文献中的可用数据进行了比较,这些数据显示出完全良好的一致性(C)2016 ElsevierLtd。保留所有权利。

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