Development of a Pd-Ag H2-selective membrane microchannel reactor for efficient solar hydrogen production with ammonia

被引:19
作者
Xia, Qi [1 ]
Lin, Liangrui [1 ]
Lin, Zihan [1 ]
Chen, Chen [1 ,2 ,3 ]
Jin, Weiya [1 ]
Liu, Qibin [2 ]
机构
[1] Zhejiang Univ Technol, Coll Mech Engn, Hangzhou 310032, Zhejiang, Peoples R China
[2] Chinese Acad Sci, Inst Engn Thermophys, Beijing 100049, Peoples R China
[3] Univ Chinese Acad Sci, 19 A Yuquan Rd, Beijing 100049, Peoples R China
基金
中国国家自然科学基金;
关键词
Solar; Ammonia; Membrane; Microchannel; THERMOCHEMICAL ENERGY-STORAGE; DECOMPOSITION;
D O I
10.1016/j.enconman.2022.116181
中图分类号
O414.1 [热力学];
学科分类号
摘要
Ammonia is one of the most promising hydrogen carriers, which realizes storing and releasing hydrogen with ammonia synthesis and decomposition, respectively. Solar-driven ammonia decomposition is a carbon-free way to release hydrogen with solar energy. Recently, there have been lots of researches conducted to enhance the conversion of ammonia decomposition including improving noble-metal-based catalysts and developing mem-brane reactors. However, critical information regarding the reactor efficiency under solar radiation is hardly provided. Additionally, the heat and mass transfer process in the membrane reactor under the solar radiation need be further enhanced for an efficient thermochemical conversion. In this paper, a novel solar driven ammonia decomposition microchannel reactor integrating with palladium-argentum hydrogen-selective mem-brane is proposed. The reactor is not only with enhanced heat and mass transfer performance but also improved conversion by separating hydrogen simultaneously. A two-dimensional membrane microchannel reactor model has been developed to study the proposed reactor. The model has been validated by comparing the model -predicted results with the experimental data from references. Moreover, the effects of reactor inlet tempera-ture, sweep gas flow rate, ammonia flow rate and retentate layer height on the reactor performance have been investigated parametrically. Learned from the results, the maximum conversion of 91% does not correspond to the maximum thermochemical conversion efficiency or overall energy efficiency, which are 23.1% and 30.7%, respectively. The maximum thermochemical conversion efficiency of 23.3% and overall energy efficiency of 31.0% have been obtained. The study provides valuable information regarding the thermochemical performance of the novel solar membrane microchannel reactor. Further, the meaningful investigations of judging if mass and heat transfer limitations occur are presented.
引用
收藏
页数:11
相关论文
共 18 条
[1]   H2 production via ammonia decomposition in a catalytic membrane reactor [J].
Cechetto, Valentina ;
Di Felice, Luca ;
Medrano, Jose A. ;
Makhloufi, Camel ;
Zuniga, Jon ;
Gallucci, Fausto .
FUEL PROCESSING TECHNOLOGY, 2021, 216
[2]   Hydrogen production from water gas shift reactions in association with separation using a palladium membrane tube [J].
Chen, Wei-Hsin ;
Lu, Jau-Jang .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2012, 36 (03) :346-354
[3]   Performance evaluation of a high-throughput microchannel reactor for ammonia decomposition over a commercial Ru-based catalyst [J].
Chiuta, Steven ;
Everson, Raymond C. ;
Neomagus, Hein W. J. P. ;
Bessarabov, Dmitri G. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (07) :2921-2926
[4]   A Review of Ammonia-Based Thermochemical Energy Storage for Concentrating Solar Power [J].
Dunn, Rebecca ;
Lovegrove, Keith ;
Burgess, Greg .
PROCEEDINGS OF THE IEEE, 2012, 100 (02) :391-400
[5]  
HARRISON RH, 1953, CHEM ENG PROG, V49, P349
[6]   Novel hollow fiber membrane reactor for high purity H2 generation from thermal catalytic NH3 decomposition [J].
Jiang, Ji ;
Dong, Qiaobei ;
McCullough, Katherine ;
Lauterbach, Jochen ;
Li, Shiguang ;
Yu, Miao .
JOURNAL OF MEMBRANE SCIENCE, 2021, 629
[7]   Hydrogen storage materials for hydrogen and energy carriers [J].
Kojima, Yoshitsugu .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (33) :18179-18192
[8]   Developing ammonia based thermochemical energy storage for dish power plants [J].
Lovegrove, K ;
Luzzi, A ;
Soldiani, I ;
Kreetz, H .
SOLAR ENERGY, 2004, 76 (1-3) :331-337
[9]   The first ammonia based solar thermochemical energy storage demonstration [J].
Lovegrove, K ;
Kreetz, H ;
Luzzi, A .
JOURNAL DE PHYSIQUE IV, 1999, 9 (P3) :581-586
[10]   A solar-driven ammonia-based thermochemical energy storage system [J].
Lovegrove, K ;
Luzzi, A ;
Kreetz, H .
SOLAR ENERGY, 1999, 67 (4-6) :309-316