摘要
The effects of reactions, different paraffins as reactants, and different zeolites as catalysts on the cracking-desulfurization of thiophene contained paraffins were studied. Low temperature, low space, velocity, and high catalyst/oil ratio were found to favor the cracking-desulfurization reaction. The activities of different zeolites for the cracking-desulfurization reaction were attenuated in the following order: HY, Hβ, and HZSM-5. The cracking of thiophene was closely related to the paraffin used and to its cracking ability. The reaction conditions, which favored the hydrogen transfer reaction, also promoted the cracking-desulfurization of thiophene.
| 源语言 | 英语 |
|---|---|
| 页(从-至) | 58-62 |
| 页数 | 5 |
| 期刊 | Petroleum Processing and Petrochemicals |
| 卷 | 31 |
| 期 | 3 |
| 出版状态 | 已出版 - 3月 2000 |
| 已对外发布 | 是 |
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