摘要
Ni-La catalysts supported on cordierite for steam reforming of kerosene to synthesis gas were prepared. Catalysts were evaluated in fixed-bed reactor under different conditions. Influence of NiO content on activity and stability of catalysts was studied. Effect of calcination temperature on catalyst activity was obvious. Mass fraction of NiO in catalyst 25% was optimal for reforming reaction. Optimal reaction conditions were 773 K and 2300/hr space velocity. Nickel on catalyst surface was in state of highly dispersed compound.
| 源语言 | 英语 |
|---|---|
| 页(从-至) | 710-713 |
| 页数 | 4 |
| 期刊 | Petrochemical Technology |
| 卷 | 34 |
| 期 | 8 |
| 出版状态 | 已出版 - 15 8月 2005 |
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