Kim, Dae Hyun Ryu, Jong Woo Choi, Eun Hyung Gong, Gyeong Taek Lee, Hyunjoo Lee, Byung Gwon Moon, Dong Ju 2024-01-20T23:01:58Z 2024-01-20T23:01:58Z 2021-09-03 2008-07-31 0920-5861 https://pubs.kist.re.kr/handle/201004/133307 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. English ELSEVIER PARTIAL OXIDATION GASOLINE HYDROGEN VEHICLES Production of synthesis gas by autothermal reforming of iso-octane and toluene over metal modified Ni-based catalyst Article 10.1016/j.cattod.2008.02.021 1 CATALYSIS TODAY, v.136, no.3-4, pp.266 - 272 CATALYSIS TODAY 136 3-4 266 272 scie scopus 000257015200011 2-s2.0-44449102589 Chemistry, Applied Chemistry, Physical Engineering, Chemical Chemistry Engineering Article; Proceedings Paper PARTIAL OXIDATION GASOLINE HYDROGEN VEHICLES ATR iso-octane gasoline fuel processor Ni-based catalyst syngas production hydrogen station