Steam reforming of ethanol over Ni-based catalysts: Effect of feed composition on catalyst stability

被引:24
作者
Trane-Restrup, R. [1 ]
Dahl, S. [2 ]
Jensen, A. D. [1 ]
机构
[1] Tech Univ Denmark, Dept Chem & Biochem Engn, DK-2800 Lyngby, Denmark
[2] Tech Univ Denmark, Dept Phys, DK-2800 Lyngby, Denmark
关键词
Steam reforming; Ethanol; Nickel; Carbon deposition; Oxygen addition; Hydrogen addition; HYDROGEN-PRODUCTION; FAST PYROLYSIS; BIO-OIL; RENEWABLE HYDROGEN; PARTIAL OXIDATION; CARBON FORMATION; SYNTHESIS GAS; ACETIC-ACID; BIOMASS; TEMPERATURE;
D O I
10.1016/j.ijhydene.2014.03.107
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
In this work the effects of steam-to-carbon ratio (S/C), and addition of H-2 or O-2 to the feed on the product yields and carbon deposition in the steam reforming (SR) of ethanol over Ni/MgAl2O4, Ni/Ce0.6Zr0.4O2, and Ni/CeO2 at 600 degrees C have been investigated. Increasing the S/C-ratio from 1.6 to 8.3 over Ni/MgAl2O4 increased conversion of ethanol as well as the yield of H-2, while the carbon deposition and yield of hydrocarbons decreased. Oxygen addition at S/C-ratio of 6 over Ni/MgAl2O4, Ni/Ce0.6Zr0.4O2, and Ni/CeO2 increased conversion, decreased the yield of hydrocarbons, and led to a decrease in the carbon deposition. Carbon deposition was almost eliminated over Ni/MgAl2O4 and Ni/Ce0.6Zr0.4O2 at an O/C-ratio of roughly 0.8 or higher. The penalty of adding O-2 was a decrease in the yield of H-2 from 70% at O/C = 0 to 50% at O/C = 0.8-1. A 90 h test at O/C = 1.1, S/C = 6, and 600 degrees C over Ni/MgAl2O4 showed stable behavior and an average rate of carbon deposition of less than 7 mu g C/g(Cat) h. The results indicate that stable operation of ethanol SR is only possible under oxidative conditions. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:7735 / 7746
页数:12
相关论文
共 55 条
[51]  
Trinh TN, ENERGY FUELS
[52]   Thermodynamic analysis of hydrogen production via autothermal steam reforming of selected components of aqueous bio-oil fraction [J].
Vagia, Ekaterini Ch. ;
Lemonidou, Anyeliki A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (10) :2489-2500
[53]   Fast pyrolysis technology development [J].
Venderbosch, R. H. ;
Prins, W. .
BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR, 2010, 4 (02) :178-208
[54]   Biomass to hydrogen via fast pyrolysis and catalytic steam reforming of the pyrolysis oil or its fractions [J].
Wang, D ;
Czernik, S ;
Montane, D ;
Mann, M ;
Chornet, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) :1507-1518
[55]   Review of biomass pyrolysis oil properties and upgrading research [J].
Zhang Qi ;
Chang Jie ;
Wang Tiejun ;
Xu Ying .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (01) :87-92