Effect of Ni/Al atomic ratio of mesoporous Ni-Al2O3 aerogel catalysts on their catalytic activity for hydrogen production by steam reforming of liquefied natural gas (LNG)

被引:30
作者
Seo, Jeong Gil [1 ]
Youn, Min Hye [2 ]
Bang, Yongju [1 ]
Song, In Kyu [1 ]
机构
[1] Seoul Natl Univ, Sch Chem & Biol Engn, Inst Chem Proc, Seoul 151744, South Korea
[2] Honam Petrochem Corp, Daeduk Res Inst, Taejon 305726, South Korea
关键词
Hydrogen production; Steam reforming of liquefied natural gas; Mesoporous nickel-alumina aerogel catalyst; Ni/Al atomic ratio; SUPPORTED NI CATALYSTS; SMALL MOO3 ADDITIONS; X-RAY PHOTOELECTRON; NICKEL-CATALYSTS; CARBON DEPOSITION; PARTIAL OXIDATION; ALUMINA; METHANE; PROPANE; COKING;
D O I
10.1016/j.ijhydene.2010.08.094
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
Mesoporous Ni-Al2O3 (xNiAE) aerogel catalysts with different Ni/Al atomic ratio (X) were prepared by a single step sol gel method and a subsequent CO2 supercritical drying method The effect of Ni/Al atomic ratio of mesoporous XNiAE aerogel catalysts on their physicochemical properties and catalytic activity for steam reforming of liquefied natural gas (LNG) was investigated Textural properties and chemical properties of XNiAE catalysts were strongly influenced by Ni/Al atomic ratio Nickel species were highly dispersed on the surface of XNiAE catalysts through the formation of surface nickel aluminate phase In the steam reforming of LNG both LNG conversion and hydrogen yield showed volcano shaped curves with respect to Ni/Al atomic ratio Average nickel diameter of XNiAl catalysts was well correlated with LNG conversion and hydrogen yield over the catalysts Among the catalysts tested 0 35NiAE (Ni/Al = 0 35) catalyst with the smallest average nickel diameter showed the best catalytic performance The highest surface area, the largest pore volume the largest average pore size and the highest reducibility of 0 35NiAE catalyst were also partly responsible for its superior catalytic performance (C) 2010 Professor T Nejat Veziroglu Published by Elsevier Ltd All rights reserved
引用
收藏
页码:12174 / 12181
页数:8
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