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Evaluation of hydrogen production with iron-based chemical looping fed by different biomass

机译:用不同生物量喂养铁基化学循环的氢气生产评价

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In this study, the iron-based chemical looping process driven by various biomasses for hydrogen production purposes is studied and evaluated thermodynamically through energy and exergy approaches. The overall system consists of some key units (combustor, reducers and oxidizer) a torrefier, a drying chamber, an air separation unit, a heat exchanger, and auxiliary units as well. The biomasses considered are first dried and torrified in the drying chamber and sent to reactors to produce hydrogen. The exergy and energy efficiencies of the iron based chemical looping facility are investigated comparatively for performance evaluation. The maximum exergy destruction and entropy production rates are calculated for the torrefaction process as 123.15 MW and 4926 kW/K respectively. Under the steady-state conditions, a total of 8 kg/s hydrogen is produced via chemical looping process. The highest energy efficiency is obtained in the looping of rice husk with 86% while the highest exergy efficiency is obtained in the looping using sugarcane bagasse with 91%, respectively. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:在该研究中,通过能量和暴露的方法研究并评估了由各种生物量驱动的用于氢生产目的的铁基化学环化过程。整体系统包括一些关键单元(燃烧器,减速器和氧化剂)镀托弗,干燥室,空气分离单元,热交换器和辅助单元。首先将所考虑的生物质在干燥室中干燥并雾化,并送至反应器以产生氢。对绩效评估进行了对基于铁基化学循环设施的漏洞和能量效率。将烘焙过程分别计算为123.15 MW和4926 kW / k的最大漏洞破坏和熵生产率。在稳态条件下,通过化学环化方法生产总共8kg / s氢气。在稻壳的环循环中获得最高能量效率,而86%,含有91%的甘蔗棒中的甘蔗棒中获得最高的高效率。 (c)2020氢能源出版物LLC。 elsevier有限公司出版。保留所有权利。

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