Reformer and Membrane Modules for Methane Conversion: Experimental Assessment and Perspectives of an Innovative Architecture

被引:15
作者
De Falco, Marcello [2 ]
Salladini, Annarita [3 ]
Iaquaniello, Gaetano [1 ]
机构
[1] Tecnimont KT SpA, I-00148 Rome, Italy
[2] Univ Campus Biomed Rome, Fac Engn, I-00128 Rome, Italy
[3] Proc Innovat SrL, I-67100 Laquila, Italy
关键词
hydrogen; industrial chemistry; membranes; palladium; steam reforming; PALLADIUM MEMBRANE; PD-AG; ALLOY MEMBRANES; HYDROGEN; REACTOR; SEPARATION; PURIFICATION; ELECTROLESS; SIMULATION; VARIABLES;
D O I
10.1002/cssc.201100009
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
An innovative concept for steam methane reforming (SMR), based on reformer and membrane modules (RMMs), has been developed and tested to investigate its performance, in terms of feed conversion, on an industrial scale. A major benefit of the proposed RMM configuration is a shift of the chemical equilibrium of SMR reactions, achieved by removing the hydrogen produced at high temperature through the integration of highly selective palladium-based membranes, which enhances the yield of product. In this manner the process can operate at temperatures as low as 600-650 degrees C, compared to the 850-880 degrees C range used in conventional plants, and allows for the use of a low-temperature heat source. This Full Paper discusses experimental data on feed conversion at different operating parameters, gathered during 1000 h of testing, and processes these data to optimize the overall architecture, defining the maximum achievable feed conversion. An overall conversion of 59% is achieved with two-step reactions at a reforming temperature of 620 degrees C. A conversion as high as 90% can be obtained with a three-step architecture at 650 degrees C by properly extending the design parameters within reasonable limits.
引用
收藏
页码:1157 / 1165
页数:9
相关论文
共 33 条
[1]   Hydrogen membrane separation techniques [J].
Adhikari, S ;
Fernando, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (03) :875-881
[2]   Efficient production of hydrogen from natural gas steam reforming in palladium membrane reactor [J].
Chen, Yazhong ;
Wang, Yuzhong ;
Xu, Hengyong ;
Xiong, Guoxing .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2008, 81 (3-4) :283-294
[3]   Pd/Ag-based membrane reactors on small scale: Assessment of the feed pressure and design parameters effect on the performance [J].
Chiappetta, G. ;
Barbieri, G. ;
Drioli, E. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2010, 49 (07) :722-731
[4]   Reformer and membrane modules plant powered by a nuclear reactor or by a solar heated molten salts: Assessment of the design variables and production cost evaluation [J].
De Falco, M. ;
Barba, D. ;
Cosenza, S. ;
Laquaniello, G. ;
Marrelli, L. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (20) :5326-5334
[5]   The effect of heat-flux profile and of other geometric and operating variables in designing industrial membrane methane steam reformers [J].
De Falco, M. ;
Nardella, P. ;
Marrelli, L. ;
Di Paola, L. ;
Basile, A. ;
Gallucci, F. .
CHEMICAL ENGINEERING JOURNAL, 2008, 138 (1-3) :442-451
[6]   Experimental tests on steam reforming of natural gas in a reformer and membrane modules (RMM) plant [J].
De Falco, M. ;
Iaquaniello, G. ;
Salladini, A. .
JOURNAL OF MEMBRANE SCIENCE, 2011, 368 (1-2) :264-274
[7]   Reformer and membrane modules plant to optimize natural gas conversion to hydrogen [J].
De Falco, M. ;
Barba, D. ;
Cosenza, S. ;
Iaquaniello, G. ;
Farace, A. ;
Giacobbe, F. G. .
ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2009, 4 (03) :259-269
[8]   Pd-based membrane steam reformers: A simulation study of reactor performance [J].
De Falco, Marcello .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (12) :3036-3040
[9]  
De Falco M, 2011, MEMBRANE REACTORS FOR HYDROGEN PRODUCTION PROCESSES, P201, DOI 10.1007/978-0-85729-151-6_10
[10]  
DEFALCO M, 2009, SYNGAS PRODUCTION ME, P263