Production of synthesis gas by autothermal reforming of iso-octane and toluene over metal modified Ni-based catalyst

被引:14
作者
Kim, Dae Hyun [1 ]
Ryu, Jong Woo [1 ]
Choi, Eun Hyung [1 ]
Gong, Gyeong Taek [1 ]
Lee, Hyunjoo [1 ]
Lee, Byung Gwon [1 ]
Moon, Dong Ju [1 ]
机构
[1] Korea Inst Sci & Technol, Clean Energy Res Ctr, Seoul 130650, South Korea
关键词
ATR; iso-octane; gasoline fuel processor; Ni-based catalyst; syngas production; hydrogen station;
D O I
10.1016/j.cattod.2008.02.021
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The reforming process of gasoline is an attractive technique for fuel processor or hydrogen station applications. We investigated catalytic autothermal reforming (ATR) of iso-octane and toluene over transition metal supported catalysts. The catalysts were prepared by an incipient wetness impregnation method and characterized by N-2 physisorption, XRD, and TEM techniques before and after the reaction. Many of the tested catalysts displayed reasonably good activity towards the reforming reactions of isooctane. Especially, Ni/Fe/MgO/Al2O3 catalyst showed more activity than the other catalysts tested in this study including commercial HT catalyst. Ni/Fe/MgO/Al2O3 catalyst showed good stability for 700 h in the ATR of iso-octane. No major change was observed in catalytic activity in ATR of iso-octane or in the structure of catalyst. Since iso-octane, toluene are surrogates of gasoline, Ni/Fe/MgO/Al2O3 catalyst can be considered as ATR catalyst for gasoline fuel processor and hydrogen station systems. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:266 / 272
页数:7
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