Hydrogen from oxygenated solvents by steam reforming on Ni/Al2O3 catalyst

被引:51
作者
Palmeri, N. [1 ]
Chiodo, V. [2 ]
Freni, S. [2 ]
Frusteri, F. [2 ]
Bart, J. C. J. [1 ]
Cavallaro, S. [1 ]
机构
[1] Univ Messina, Dipartimento Chim Ind & Ingn Mat, I-98166 Sant Agata Di Messina, Italy
[2] Ist CNR ITAE, I-98126 Messina, Italy
关键词
Ethanol; Propanol; Solvents; Steam reforming; Ni catalyst;
D O I
10.1016/j.ijhydene.2008.07.064
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
Industrial wastes from the semiconductor industry comprise solvent mixtures of organic oxygenated compounds. Steam reforming of three alcohols and three oxygenated molecules (aldehydes and ketones), normally used in the electronics industry, was carried out at 1073 K by using a Ni/Al2O3 catalyst. Hydroxyl and carbonyl groups show highly different reactivities and coke formation from molecules containing a hydroxyl group is higher than for those with a carbonyl group. Thermodynamic considerations on the basis of the outlet compositions have allowed calculation of the mass action ratio (MAR) for the main equilibria involved: (i) methane steam reforming (MSR); (ii) water-gas shift reaction (WGSR); (iii) methane pyrolysis (PYR); and (iv) Boudouard reaction (BOUD). We suggest that MAR(MSR) is lower than equilibrium value and excess of methane is always present in the reaction atmosphere. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:6627 / 6634
页数:8
相关论文
共 35 条
[1]  
ALLINGER J, 1974, ORGANIC CHEM
[2]  
[Anonymous], 2020, CATAL SCI TECHNOL
[3]  
BRIONES R, 2006, 549 DEP TOX SUBST CO
[4]   Novel resin-based ultrapurification system for reprocessing IPA in the semiconductor industry [J].
Buragohain, PV ;
Gill, WN ;
Cramer, SM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (09) :3149-3154
[5]   Ethanol steam reforming in a molten carbonate fuel cell. A preliminary kinetic investigation [J].
Cavallaro, S ;
Freni, S .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1996, 21 (06) :465-469
[6]   Performance of Rh/Al2O3 catalyst in the steam reforming of ethanol:: H2 production for MCFC [J].
Cavallaro, S ;
Chiodo, V ;
Freni, S ;
Mondello, N ;
Frusteri, F .
APPLIED CATALYSIS A-GENERAL, 2003, 249 (01) :119-128
[7]   Catalytic steam reforming of chlorocarbons: trichloroethane, trichloroethylene and perchloroethylene [J].
Coute, N ;
Ortego, JD ;
Richardson, JT ;
Twigg, MV .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1998, 19 (3-4) :175-187
[8]   Hydrogen production from the fermentation of corn stover biomass pretreated with a steam-explosion process [J].
Datar, Rohit ;
Huang, Jie ;
Maness, Pin-Ching ;
Mohagheghi, Ali ;
Czemik, Stefan ;
Chornet, Esteban .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (08) :932-939
[9]   Electricity from ethanol fed SOFCs: the expectations for sustainable development and technological benefits [J].
Douvartzides, SL ;
Coutelieris, FA ;
Demin, AK ;
Tsiakaras, PE .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2004, 29 (04) :375-379
[10]   Exergy analysis of a solid oxide fuel cell power plant fed by either ethanol or methane [J].
Douvarzides, S ;
Coutelieris, F ;
Tsiakaras, P .
JOURNAL OF POWER SOURCES, 2004, 131 (1-2) :224-230