| FX-01催化剂上苯与二乙苯烷基转移 |
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| 作者单位： | ：北京服装学院化工研究所,北京 100029 |
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| 摘 要： | The kinetics of diethylbenzene transalkylationwith benzene over FX-01 catalyst has been studied,and the rate equation has beenobtained.The model for liquid-solid fixed-bed reactor for producing 15 000 tonsethylbenzne per year is proposed based on this rate equation.The technical dimensions ofthe reactor arediameter 0.35 m,height 9 m,catalyst load 486 kg.The appropriateoperating conditions aretemperature 250～260 ℃,WHSV of total feedstock over 5 h－1and feed molar ratio of benzene-to-diethylbenzene 8／1～12／1.
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| 关 键 词： | transalkylation kinetics diethylbenzene zeolite catalyst |
| 修稿时间： | 1998-02-20 |
Transalkylationof Diethylbenzene with Benzene over FX-01 Zeolite Catalyst |
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