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Autothermal-reformation enhancement using a stratified-catalyst technique

机译:使用分层催化剂技术增强自热重整

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An investigation of a stratified catalyst arrangement for methanol autothermal reforming was conducted. The stratified arrangement consisted of a monolith platinum group metal (PGM) catalyst, immediately followed by a pelletized Cu/ZnO/Al2O3 water gas shift (WGS) catalyst. The system was experimentally investigated under different test conditions by varying the flow rate, oxygen-to-carbon ratio, and the packed length of the downstream WGS bed. The reactor performance was quantified with several metrics including the fuel conversion, hydrogen yield, system temperatures, and preliminary results are shown for short-term catalyst degradation. Conversion and hydrogen yield increased significantly at low oxygen-to-carbon ratios as compared to the stand-alone PGM catalyst. Results confirm the benefits of using a PGM and WGS catalyst in a stratified fashion and the stratified arrangement increases performance over each of the catalysts used singularly. Further study is warranted considering potential degradation of the WGS bed caused by high temperatures encountered at the exit of the PGM section. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:对用于甲醇自热重整的分层催化剂装置进行了研究。分层结构由整体式铂族金属(PGM)催化剂组成,紧接着是制粒的Cu / ZnO / Al2O3水煤气变换(WGS)催化剂。通过改变流速,氧碳比和下游WGS床的填充长度,在不同的测试条件下对该系统进行了实验研究。反应器性能通过多种指标进行了量化,包括燃料转化率,氢气产率,系统温度,并显示了短期催化剂降解的初步结果。与独立的PGM催化剂相比,在低氧碳比下,转化率和氢气产率显着提高。结果证实了以分层方式使用PGM和WGS催化剂的好处,并且分层布置相对于单独使用的每种催化剂都提高了性能。考虑到在PGM部分出口处遇到的高温可能导致WGS床的潜在降解,需要进行进一步的研究。 (C)2017氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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