Steam reforming of bagasse to hydrogen and synthesis gas using ruthenium promoted Ni-Fe/γ-Al2O3nano-catalysts

被引:28
作者
Jafarian, Sajedeh [1 ]
Tavasoli, Ahmad [1 ]
Karimi, Ali [2 ]
Norouzi, Omid [1 ]
机构
[1] Univ Tehran, Sch Chem, Coll Sci, Tehran, Iran
[2] Res Inst Petr Ind, Gas Div, Tehran, Iran
关键词
Biomass gasification; Steam reforming; Hydrogen; Nickel; Iron; Ruthenium; SUPERCRITICAL WATER GASIFICATION; CATALYTIC PERFORMANCE; NI CATALYSTS; PYROLYSIS; ETHANOL; TAR;
D O I
10.1016/j.ijhydene.2016.05.261
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
Bagasse conversion to H-2, CO and light gaseous hydrocarbons was performed in a batch micro reactor under 850 degrees C and atmospheric pressure in the presence of unpromoted and ruthenium promoted Ni-Fe/gamma-Al2O3 nano catalysts. The nano catalysts were prepared with 12 wt.% Ni, 6 wt.% Fe and 0.5 to 2 wt.% Ru loadings via microemulsion technique. The catalysts were extensively characterized using ICP, XRD, TPR, BET, TEM and H-2 chernisorption techniques. XRD patterns confirmed formation of Ni Fe alloys on the catalysts. Ruthenium increased dispersion of active metal clusters by 44.6% and consequently improved the reducibility of the catalysts. The addition of 1 wt.% Ru increased the total gas yield, the yield of hydrogen, the yield of carbon monoxide and the carbon conversion efficiency by 34.2%, 35.9%, 33.54% and 44% respectively. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:5505 / 5512
页数:8
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