Hydrogen production from methane and natural gas steam reforming in conventional and microreactor reaction systems

被引:115
作者
Izquierdo, U. [1 ]
Barrio, V. L. [1 ]
Cambra, J. F. [1 ]
Requies, J. [1 ]
Gueemez, M. B. [1 ]
Arias, P. L. [1 ]
Kolb, G. [2 ]
Zapf, R. [2 ]
Gutierrez, A. M. [3 ]
Arraibi, J. R. [3 ]
机构
[1] Univ Basque Country UPV EHU, Fac Engn, Bilbao 48013, Spain
[2] Inst Mikrotech Mainz GmbH, D-55129 Mainz, Germany
[3] Nat Gas Energia Distribuc, Bilbao 48001, Spain
关键词
Hydrogen; Microreactor; Natural gas; Methane; Steam reforming; CATALYSTS; PROPANE; FUEL;
D O I
10.1016/j.ijhydene.2011.11.048
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
Ni-based (over MgO and Al2O3) and noble metal-based (Pd and Pt over Al2O3) catalysts were prepared by wet impregnation method and thereafter impregnated in microreactors. The catalytic activity was measured at several temperatures, atmospheric pressure and different steam to carbon, S/C, ratios. These conditions were the same for conventional, fixed bed reactor system, and microreactors. Weight hourly space velocity, WHSV, was maintained equal in order to compare the activity results from both reaction systems. For microreactor systems, similar activities of Ni-based catalyst were measured in the steam methane reforming (SMR) activity tests, but not in the case of natural gas steam reforming tests. When noble metal-based catalysts were used in the conventional reaction system no significant activity was measured but all catalysts showed some activity when they were tested in the microreactor systems. The analysis by SEM and TEM revealed a carbon-free surface for Ni-based catalyst as well as carbon filaments growth in case of noble metal-based catalysts. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:7026 / 7033
页数:8
相关论文
共 25 条
[1]   Water effect in hydrogen production from methane [J].
Acha, E. ;
Requies, J. ;
Barrio, V. L. ;
Cambra, J. F. ;
Gueemez, M. B. ;
Arias, P. L. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (20) :11525-11532
[2]   The future of hydrogen - opportunities and challenges [J].
Ball, Michael ;
Wietschel, Martin .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (02) :615-627
[3]   Policies for the transition towards a hydrogen economy: The EU case [J].
Bleischwitz, Raimund ;
Bader, Nikolas .
ENERGY POLICY, 2010, 38 (10) :5388-5398
[4]   Co2e emissions abatement costs of reducing natural gas flaring in Brazil by investing in offshore GTL plants producing premium diesel [J].
Castelo Branco, David A. ;
Szklo, Alexandre S. ;
Schaeffer, Roberto .
ENERGY, 2010, 35 (01) :158-167
[5]   Coating of steam reforming catalysts in non-porous multi-channeled microreactors [J].
Conant, Travis ;
Karim, Ayman ;
Datye, Abhaya .
CATALYSIS TODAY, 2007, 125 (1-2) :11-15
[6]   Comparison between conventional fixed-bed and microreactor technology for a portable hydrogen production case [J].
Delsman, ER ;
Laarhoven, BJPF ;
de Croon, MHJM ;
Kramer, GJ ;
Schouten, JC .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2005, 83 (A9) :1063-1075
[7]  
Fogler H. S, 1999, ELEMENTS CHEM REACTI, V3rd
[8]   Nanostructured Pt- and Ni-based catalysts for CO2-reforming of methane [J].
Garcia-Dieguez, M. ;
Pieta, I. S. ;
Herrera, M. C. ;
Larrubia, M. A. ;
Alemany, L. J. .
JOURNAL OF CATALYSIS, 2010, 270 (01) :136-145
[9]   Characterization of alumina-supported Pt, Ni and PtNi alloy catalysts for the dry reforming of methane [J].
Garcia-Dieguez, Monica ;
Finocchio, Elisabetta ;
Angeles Larrubia, Maria ;
Alemany, Luis J. ;
Busca, Guido .
JOURNAL OF CATALYSIS, 2010, 274 (01) :11-20
[10]   Preparation and characterization of porous alumina-based catalyst coatings in microchannels [J].
Germani, G. ;
Stefanescu, A. ;
Schuurman, Y. ;
van Veen, A. C. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (18-20) :5084-5091