共 14 条
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.
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页码:266 / 272
页数:7
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