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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received July 11, 2017
Accepted February 22, 2018
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Conceptual feasibility studies of a COX-free hydrogen production from ammonia decomposition in a membrane reactor for PEM fuel cells

Department of Advanced Materials and Chemical Engineering, Catholic University of Daegu, 13-13 Hayang-ro, Hayang-yep, Gyeongsan, Gyeongbuk 38430, Korea
hklim@cu.ac.kr
Korean Journal of Chemical Engineering, July 2018, 35(7), 1509-1516(8), 10.1007/s11814-018-0037-5
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Abstract

COX-free hydrogen production from ammonia decomposition in a membrane reactor (MR) for PEM fuel cells was studied using a commercial chemical process simulator, Aspen HYSYS®. With process simulation models validated by previously reported kinetics and experimental data, the effect of key operating parameters such as H2 permeance, He sweep gas flow, and operating temperature was investigated to compare the performance of an MR and a conventional packed-bed reactor (PBR). Higher ammonia conversions and H2 yields were obtained in an MR than ones in a PBR. It was also found that He sweep gas flow was favorable for XNH3 enhancement in an MR with a critical value (5 kmol h-1), above which no further effect was observed. A higher H2 permeance led to an increased H2 yield and H2 yield enhancement in an MR with the reverse effect of operating temperature on the enhancement. In addition, lower operating temperature resulted in higher XNH3 enhancement and H2 yield enhancement as well as NG cost savings in a MR compared to a conventional PBR.

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