Ammonia decomposition for hydrogen production using packed bed catalytic membrane reactor

被引:12
|
作者
Nailwal, B. C. [1 ]
Chotalia, P. [2 ]
Salvi, J. [2 ]
Goswami, N. [1 ]
Muhmood, L. [2 ]
Adak, A. K. [1 ]
Kar, Soumitra [1 ,3 ]
机构
[1] Bhabha Atom Res Ctr, Desalinat & Membrane Technol Div, Mumbai 400085, India
[2] KJ Somaiya Coll Engn, Mumbai 400077, India
[3] Homi Bhabha Natl Inst, Mumbai 400094, India
关键词
Hydrogen; Ammonia decomposition; Membrane reactor; CFD simulations; HI DECOMPOSITION; NUMERICAL SIMULATIONS; FUEL-CELLS; STORAGE; ENERGY; SEPARATION;
D O I
10.1016/j.ijhydene.2023.09.229
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Ammonia can be used for hydrogen storage as it is relatively easy to transport, and can be generated at the site by decomposition of ammonia. In this work, the authors report studies on ammonia decomposition using packed-bed catalytic membrane reactor (PBCMR) based on Pd-Ag alloy membrane. The studies were carried out at different operating conditions in single tube PBCMR as well as in packed bed catalytic reactor without membrane (PBCR). A conversion of-93% was achieved in PBCMR at a temperature of 773 K and 1 bar, as against a conversion of-80% in PBCR. A CFD model was also developed and validated using experimental results. The model was further extrapolated to carry out 3D simulations of multi-tube PBCMR for parametric optimisation. This is a first of its kind study wherein a computational approach is used for studies on ammonia decomposition using multi-tube PBCMR.(c) 2023 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:1272 / 1287
页数:16
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