石油化工高等学校学报

石油化工高等学校学报 ›› 2013, Vol. 26 ›› Issue (1): 36-39.DOI: 10.3969/j.issn.1006396X.2013.01.009

• 石油化工 • 上一篇    下一篇

160kg/hC16-C19重烷烯烷基化中试装置工艺研究

卢瑞真,王德慧,赵德智*   

  1. (辽宁石油化工大学石油化工学院,辽宁抚顺113001)
  • 收稿日期:2012-11-07 出版日期:2013-02-25 发布日期:2013-02-25
  • 作者简介:卢瑞真(1987飊),女,河北衡水市,在读硕士。

Pilot Plant Study for 160 kg/h C16C19 ReAlkylene Alkylation Process

  1. (School of Petrochemical Engineering, Liaoning Shihua University, Fushun Liaoning 113001, China)
  • Received:2012-11-07 Published:2013-02-25 Online:2013-02-25

摘要: 采用氢氟酸烷基化法(UOP法),对C16-C19的重烷烯烃进行烷基化实验,取得相关工艺数据,开发重烷烯烷基化中试工艺技术,为工业化提供相关基础数据。当反应温度为50℃,压力为0.88 MPa,反应时间为20 min,苯烯物质的量比为8:1,HF和碳氢化合物的体积比为2:1时,得到其最佳转化率为10.4%。

关键词: 重烷烯, 烷基化, 暋中试装置 , 工艺流程

Abstract: With the method of hydrofluoric acidalkylation(the UOP method), realkylene(C16C19) was reacted. By this reaction, the relevant process data was obtained, the alkylation pilot technology was developed, and the underlying industrialized data was provided. When the reaction temperature is 50 ℃, the reaction pressure is 0.88 MPa, reaction time is 20 min, the amount of substance ratio for benzene and heavy hydride olefinic is 8∶1 and the volume ratio for HF and hydrocarbon is 2∶1, the conversion rate can be the best for 10.4%.

Key words: Realkylene,    ,  Alkylation,     ,  Pilot means,   ,  Process

引用本文

卢瑞真,王德慧,赵德智. 160kg/hC16-C19重烷烯烷基化中试装置工艺研究[J]. 石油化工高等学校学报, 2013, 26(1): 36-39.

LU Ruizhen, WANG Dehui, ZHAO Dezhi. Pilot Plant Study for 160 kg/h C16C19 ReAlkylene Alkylation Process[J]. Journal of Petrochemical Universities, 2013, 26(1): 36-39.

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