摘要
Hydrogenation of ethyne on γ-Mo2N was investigated using a fixed-bed continuous flow micro-reactor. 95% of ethyne conversion and 80% of ethene selectivity were obtained at 150 °C and 3 000 h-1. The distribution of the products remained almost unchanged with varying reaction temperature and space velocity. These results are different from that obtained on Pd/Al2O3. Under the similar reaction conditions the main product is ethane and the distribution of the products varies with the reaction temperature and space velocity over Pd/Al2O3. The results were explained by Bond model, and firmly held hydrocarbon adspecies may be responsible for the high selectivity for ethene.
| 源语言 | 英语 |
|---|---|
| 页(从-至) | 220 |
| 页数 | 1 |
| 期刊 | Chinese Journal of Catalysis |
| 卷 | 21 |
| 期 | 3 |
| 出版状态 | 已出版 - 2000 |
| 已对外发布 | 是 |
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