Theoretical Study of a Membrane Reactor for the Water Gas Shift Reaction Under Nonisothermal Conditions

被引:17
作者
Adrover, Maria E. [1 ]
Lopez, Eduardo [1 ]
Borio, Daniel O. [1 ]
Pedernera, Marisa N. [1 ]
机构
[1] Univ Nacl Sur, CONICET, PLAPIQUI, Dept Chem Engn, RA-8000 Bahia Blanca, Buenos Aires, Argentina
关键词
membrane reactors; water gas shift; Pd membrane; thermal effects; CERAMIC MEMBRANES; PACKED-BEDS; SIMULATION; PD; PERFORMANCE; PARAMETERS; OPERATION;
D O I
10.1002/aic.11929
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A simulation of a membrane reactor for the water gas shift reaction is carried out by means of a 1D pseudo-homogeneous nonisothermal mathematical model. The composite membrane consists of a dense layer of Pd (selective to H-2) supported over a porous ceramic layer. The effect of temperature, overall heat-transfer coefficient, and mode of operation on the membrane reactor performance and stability are analyzed, and the results obtained are compared with those corresponding to a reactor with no hydrogen permeation. (C) 2009 American Institute of Chemical Engineers AIChE J, 55: 3206-3213, 2009
引用
收藏
页码:3206 / 3213
页数:8
相关论文
共 22 条
[1]   Modeling of a novel membrane reactor to integrate dehydrogenation of ethylbenzene to styrene with hydrogenation of nitrobenzene to aniline [J].
Abo-Ghander, Nabeel S. ;
Grace, John R. ;
Elnashaie, Said S. E. H. ;
Lim, C. Jim .
CHEMICAL ENGINEERING SCIENCE, 2008, 63 (07) :1817-1826
[2]   Engineering evaluations of a catalytic membrane reactor for the water gas shift reaction [J].
Barbieri, G ;
Brunetti, A ;
Granato, T ;
Bernardo, P ;
Drioli, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (20) :7676-7683
[3]   Co-current and counter-current modes for water gas shift membrane reactor [J].
Basile, A ;
Paturzo, L ;
Gallucci, F .
CATALYSIS TODAY, 2003, 82 (1-4) :275-281
[4]   Experimental and simulation of both Pd and Pd/Ag for a water gas shift membrane reactor [J].
Basile, A ;
Chiappetta, G ;
Tosti, S ;
Violante, V .
SEPARATION AND PURIFICATION TECHNOLOGY, 2001, 25 (1-3) :549-571
[5]  
BRATCH M, 1997, ENERGY CONVERSION MA, V38, P159
[6]   Simulation study of water gas shift reaction in a membrane reactor [J].
Brunetti, A. ;
Caravella, A. ;
Barbieri, G. ;
Drioli, E. .
JOURNAL OF MEMBRANE SCIENCE, 2007, 306 (1-2) :329-340
[7]   Theoretical analysis of the effect of catalyst mass distribution and operation parameters on the performance of a Pd-based membrane reactor for water-gas shift reaction [J].
Chiappetta, Giovanni ;
Clarizia, Gabriele ;
Drioli, Enrico .
CHEMICAL ENGINEERING JOURNAL, 2008, 136 (2-3) :373-382
[8]   Catalytic reactors based on porous ceramic membranes [J].
Coronas, J ;
Santamaría, J .
CATALYSIS TODAY, 1999, 51 (3-4) :377-389
[9]   An analysis of the performance of membrane reactors for the water-gas shift reaction using gas feed mixtures [J].
Criscuoli, A ;
Basile, A ;
Drioli, E .
CATALYSIS TODAY, 2000, 56 (1-3) :53-64
[10]   Simulation of large-scale membrane reformers by a two-dimensional model [J].
De Falco, M. ;
Di Paola, L. ;
Marrelli, L. ;
Nardella, P. .
CHEMICAL ENGINEERING JOURNAL, 2007, 128 (2-3) :115-125