CFD simulations of coupled, countercurrent combustor/reformer microdevices for hydrogen production

被引:60
作者
Deshmukh, SR
Vlachos, DG [1 ]
机构
[1] Univ Delaware, Dept Chem Engn, Newark, DE 19716 USA
[2] Univ Delaware, Ctr Catalyt Sci & Technol, Newark, DE 19716 USA
关键词
D O I
10.1021/ie0490987
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Two-dimensional computational fluid dynamics (CFD) simulations are used to study spatially segregated, multifunctional, microchemical devices for hydrogen production. In particular, coupling between homogeneous propane combustion and catalytic ammonia decomposition on a Ru catalyst is studied in a microdevice consisting of alternating combustion and decomposition channels as a function of flow rate and materials conductivity in the countercurrent flow configuration. It is found that the high temperatures generated via homogeneous combustion lead to high conversions in short contact times and thus to compact devices. Different performance measures are evaluated to assess the operability of the device. Sufficiently high ammonia flow rates serve a dual purpose by lowering device temperatures and enabling the production of larger flow rates of hydrogen. Finally, it is shown that device operation is limited only to high-conductivity materials and fast ammonia flows.
引用
收藏
页码:4982 / 4992
页数:11
相关论文
共 51 条
[41]  
2-8
[42]   MEMS-based components of a miniature fuel cell/fuel reformer system [J].
Tanaka, S ;
Chang, KS ;
Min, KB ;
Satoh, D ;
Yoshida, K ;
Esashi, M .
CHEMICAL ENGINEERING JOURNAL, 2004, 101 (1-3) :143-149
[43]   Thermal and mechanical analysis of a microreactor for high temperature catalytic gas phase reactions [J].
Tiggelaar, RM ;
Loeters, PWH ;
van Male, P ;
Oosterbroek, RE ;
Gardeniers, JGE ;
de Croon, MHJM ;
Schouten, JC ;
Elwenspoek, MC ;
van den Berg, A .
SENSORS AND ACTUATORS A-PHYSICAL, 2004, 112 (2-3) :267-277
[44]  
VANSINT AM, 2002, CHEM ENG SCI, V57, P833
[45]   Steam reforming of methane and water-gas shift in catalytic wall reactors [J].
Venkataraman, K ;
Wanat, EC ;
Schmidt, LD .
AICHE JOURNAL, 2003, 49 (05) :1277-1284
[46]   Millisecond catalytic wall reactors: dehydrogenation of ethane [J].
Venkataraman, K ;
Redenius, JM ;
Schmidt, LD .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (13) :2335-2343
[47]  
Veser G, 2000, MICROREACTION TECHNOLOGY: INDUSTRIAL PROSPECTS, P674
[48]   SIMPLIFIED REACTION-MECHANISMS FOR THE OXIDATION OF HYDROCARBON FUELS IN FLAMES [J].
WESTBROOK, CK ;
DRYER, FL .
COMBUSTION SCIENCE AND TECHNOLOGY, 1981, 27 (1-2) :31-43
[49]   Influence of flow arrangement in catalytic plate reactors for methane steam reforming [J].
Zanfir, M ;
Gavriilidis, A .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2004, 82 (A2) :252-258
[50]   Modelling of a catalytic plate reactor for dehydrogenation-combustion coupling [J].
Zanfir, M ;
Gavriilidis, A .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (08) :2671-2683