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首页> 外文期刊>International journal of hydrogen energy >Characterization on trace carbon monoxide leakage in high purity hydrogen in sorption enhanced water gas shifting process
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Characterization on trace carbon monoxide leakage in high purity hydrogen in sorption enhanced water gas shifting process

机译:吸附增强水煤气变换过程中高纯氢中微量一氧化碳泄漏的表征

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The sorption-enhanced water-gas shift (SEWGS) reaction based on elevated-temperature CO2 adsorbent and water-gas shift (WGS) catalyst has the potential to produce fuel cell levels of H-2 from syngas directly. However, more than 20 ppm of CO could poison the Pt electrode in a proton exchange membrane fuel cell. In this paper, the outlet CO concentration of SEWGS was investigated in a fixed bed at 350-450 degrees C at 1-3 MPa. The reactor was filled with K2CO3-promoted Mg-Al hydrotalcite and high-temperature Fe-Cr WGS catalyst with a volume ratio of 5. The ratio of CO and CO2 breakthrough time tau(k) was first proposed to characterize the utilization ratio of CO2 adsorbent quantitatively. Various working conditions of SEWGS, including inlet CO concentration (5-20 Vol%), balanced gas (Ar, H2), cycle index (1-4), and S/G ratio (1.25-5), are studied. The experimental results show that CO concentration can be less than 10 ppm when the inlet gas consists of 5%-20% CO and balanced Ar. If 95% H-2 is added, a range of 147.5-205.0 ppm of CO concentration is achieved., tau(20) is between 0.34 and 0.81 in the tested conditions. The breakthrough time of CO is maintained relatively stable by changing the CO inlet concentration. There is an optimal S/ G ratio owing to the WGS thermodynamic balance and the competitive adsorption of H2O. The CO2 adsorption uptake before the breakthrough of CO increases with increasing total pressure, and the performance of SEWGS declines at temperatures above 400 degrees C. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:基于高温CO2吸附剂和水煤气变换(WGS)催化剂的吸附增强水煤气变换(SEWGS)反应具有直接从合成气生产H-2燃料电池的潜力。但是,超过20 ppm的CO可能会使质子交换膜燃料电池中的Pt电极中毒。在本文中,在1-3 MPa下于350-450摄氏度的固定床中研究了SEWGS的出口CO浓度。反应器中装有体积比为5的K2CO3促进的Mg-Al水滑石和高温Fe-Cr WGS催化剂。首先提出了CO和CO2突破时间tau(k)的比值,以表征CO2的利用率吸附剂定量。研究了SEWGS的各种工作条件,包括入口CO浓度(5-20​​ Vol%),平衡气体(Ar,H2),循环指数(1-4)和S / G比(1.25-5)。实验结果表明,当进口气体由5%-20%CO和平衡Ar组成时,CO浓度可低于10 ppm。如果添加95%的H-2,则可达到147.5-205.0 ppm的CO浓度范围。在测试条件下,tau(20)在0.34至0.81之间。通过改变一氧化碳入口浓度,一氧化碳的穿透时间可以保持相对稳定。由于WGS热力学平衡和H2O的竞争性吸附,存在最佳的S / G比。在CO突破之前,CO2的吸收吸收量随总压力的增加而增加,而SEWGS的性能在高于400摄氏度的温度下会下降。(C)2016 Hydrogen Energy Publications LLC。由Elsevier Ltd.出版。保留所有权利。

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