Experimental assessment of hydrogen separation from H2/CH4 mixtures by the "steam-iron process" in an interconnected circulating fluidized bed reactor

被引:10
作者
Herguido, J. [1 ]
Pena, J. A. [1 ]
Carazo, E. [1 ]
机构
[1] Univ Zaragoza, Aragon Inst Engn Res I3A, Catalysis Mol Separat & Reactor Engn Grp CREG, Zaragoza 50018, Spain
关键词
Hydrogen; Steam-iron; Interconnected circulating fluidized; bed reactor (ICFBR); Redox; Iron oxide; STORING HYDROGEN; REDOX PROCESS; REDUCTION; OXIDE; GAS; PARTICLES; KINETICS; SOLIDS; STAGE;
D O I
10.1016/j.ijhydene.2014.07.006
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
An experimental study devoted to the continuous separation of hydrogen from its mixtures with methane in continuous regime is presented. The study was carried out in a single-vessel reactor divided into two interconnected adjoining chambers, operating as fluidized beds and with a continuous flow of solids between them. The process is based on iron oxide being selectively reduced or oxidized, depending on the redox nature of the gas stream being fed to the respective chamber (steam-iron process or SIP). Conditions to minimize gas leakage between the interconnected beds, avoiding insufficient circulation of solids, have been experimentally determined. The effects of different interconnecting designs, spatial gas velocities and partial pressures of reactants have been tested. Also the effects of several operating parameters (primarily hydrogen content in the inlet gas stream and spatial velocities) on process efficiency have been analyzed. Accordingly, a final configuration has been proposed for stable hydrogen separation and tested for several hours of time on stream. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:14050 / 14060
页数:11
相关论文
共 28 条
[1]   The use of iron oxide as oxygen carrier in a chemical-looping reactor [J].
Abad, A. ;
Mattisson, T. ;
Lyngfelt, A. ;
Johansson, M. .
FUEL, 2007, 86 (7-8) :1021-1035
[2]   Mapping of the range of operational conditions for Cu-, Fe-, and Ni-based oxygen carriers in chemical-looping combustion [J].
Abad, Alberto ;
Adanez, Juan ;
Garcia-Labiano, Francisco ;
de Diego, Luis F. ;
Gayan, Pilar ;
Celaya, Javier .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :533-549
[3]  
Duran P, 2008, HYCELTEC S BILB SPAI
[4]   Realizing the hydrogen future:: the International Energy Agency's efforts to advance hydrogen energy technologies [J].
Elam, CC ;
Padró, CEG ;
Sandrock, G ;
Luzzi, A ;
Lindblad, P ;
Hagen, EF .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2003, 28 (06) :601-607
[5]   CONTROL MECHANISMS OF FLUIDIZED SOLIDS CIRCULATION BETWEEN ADJACENT VESSELS [J].
FOX, D ;
MOLODTSOF, Y ;
LARGE, JF .
AICHE JOURNAL, 1989, 35 (12) :1933-1941
[7]   Usage of biomass gas for fuel cells by the SIR process [J].
Hacker, V ;
Faleschini, G ;
Fuchs, H ;
Fankhauser, R ;
Simader, G ;
Ghaemi, M ;
Spreitz, B ;
Friedrich, K .
JOURNAL OF POWER SOURCES, 1998, 71 (1-2) :226-230
[8]   On the use of fluidized bed catalytic reactors where reduction and oxidation zones are present simultaneously [J].
Herguido, J ;
Menéndez, M ;
Santamaría, J .
CATALYSIS TODAY, 2005, 100 (1-2) :181-189
[9]  
Herguido J, 2005, 7 WORLD C CHEM ENG G, P316
[10]   Hydrogen from ethanol by steam iron process in fixed bed reactor [J].
Hormilleja, E. ;
Duran, P. ;
Plou, J. ;
Herguido, J. ;
Pena, J. A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (10) :5267-5273