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Electrochemical reforming vs. catalytic reforming of ethanol: A process energy analysis for hydrogen production

机译:乙醇的电化学重整与催化重整:制氢的过程能分析

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This work reports an energetic analysis for hydrogen production via catalytic steam and electrochemical ethanol reforming processes. For both systems, a complete flow diagram process was proposed and simulated by Aspen HYSYS according to literature data. Besides hydrogen, other byproducts such as acetaldehyde (electrochemical reforming) and ethylene and methane (catalytic reforming) were also considered. The energy requirement of the different process units was calculated according to the operating parameters. Just process energy (thermal energy and electrical energy) consumption was considered in the study of the steam reforming whereas both energy process and electrical energy consumption were considered in the study of the electrochemical reforming. Material balances revealed electrochemical reforming to present higher hydrogen yields. (0.0436 vs. 0.0304 kg H-2/kg C2H5OH of the classical catalytic reforming). In addition to its higher simplicity, simulation results showed a lower energy consumption in the H-2 production by the electrochemical approach (29.2 vs. 32.70 kWh/Kg of H2). These results demonstrated the interest of the electrochemical reforming of ethanol to obtain high purity hydrogen in a single reaction/separation step, thereby representing an interesting alternative to classical catalytic reforming. (C) 2015 Elsevier B.V. All rights reserved.
机译:这项工作报告了通过催化蒸汽和电化学乙醇重整过程生产氢的能量分析。对于这两个系统,提出了完整的流程图过程,并由Aspen HYSYS根据文献数据对其进行了仿真。除了氢以外,还考虑了其​​他副产物,例如乙醛(电化学重整)以及乙烯和甲烷(催化重整)。根据操作参数计算不同工艺单元的能量需求。在蒸汽重整的研究中仅考虑过程能量(热能和电能)的消耗,而在电化学重整的研究中仅考虑能量过程和电能的消耗。材料平衡表明电化学重整以呈现更高的氢产率。 (0.0436 vs.0.0304 kg H-2 / kg C2H5OH的经典催化重整)。除了具有更高的简便性外,模拟结果还显示,通过电化学方法在H-2生产中的能耗更低(29.2 vs. 32.70 kWh / Kg H2)。这些结果证明了在单个反应/分离步骤中乙醇的电化学重整以获得高纯度氢的兴趣,从而代表了经典催化重整的有趣替代。 (C)2015 Elsevier B.V.保留所有权利。

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