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费托合成高温油相产品中正构烃的分离

Separation of n-hydrocarbons from high temperature oil phase products of Fischer-Tropsch synthesis

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【作者】 王燕葛喜慧张敏卿朱怀工张子建王明

【Author】 WANG Yan;GE Xihui;ZHANG Minqing;ZHU Huaigong;ZHANG Zijian;WANG Ming;School of Chemical Engineering & Technology,Tianjin University;Yulin Chemical Branch,China Shenhua Coal to Liquid and Chemical Co.,Ltd.;Tianjin Univtech Co.,Ltd.;

【机构】 天津大学化工学院中国神华煤制油化工有限公司榆林化工分公司中国天大天久科技股份有限公司

【摘要】 以模拟的费托合成高温油相产品为原料,采用尿素包合法从原料中分离正构烃。考察了活化剂的种类、包合反应条件、解包合反应条件等对正构烃分离效果的影响。通过正交实验研究,结果表明:乙醇为较适宜的活化剂;较优反应条件为反应温度5℃,反应时间60min,以1g原料为基准,尿素用量2.75g,乙醇用量3.5mL,水用量1.125mL。在此包合反应条件下,得到1-癸烯的回收率为87.75%,正癸烷的回收率为89.90%。尿素包合物的解包合反应实验结果说明,水的存在有利于解包合反应的进行,得到正构烃回收率较高。用水量为100 mL时,尿素包合物的解包合反应基本完成。

【Abstract】 The simulated high temperature oil phase products of Fischer-Tropsch synthesis were taken as raw materials and the urea inclusion method was used to separate n-hydrocarbons from the raw materials. The effects of activators,inclusion reaction conditions and unpacked reaction conditions on n-hydrocarbons separation were studied. Orthogonal experimental study showed that ethanol was a suitable activator and the optimal reaction conditions for inclusion were:reaction temperature 5 ℃,reaction time 1h,based on 1g raw materials,amount of urea 2.75 g,amount of ethano 3.5mL,amount of water 1.125 mL. Under the optimal reaction conditions,recovery rate of 1-decene was 87.75% and that of n-decane was 89.90%. The unpacked reaction results of inclusion complex illustrated that presence of water was conducive to the unpacked reaction and recovery rate of n-hydrocarbons was higher than without water. When water consumption reached 100 mL,the unpacked reaction of inclusion complex was completed.

【基金】 国家高技术发展计划项目(2011AA05A204)
  • 【文献出处】 化工进展 ,Chemical Industry and Engineering Progress , 编辑部邮箱 ,2014年11期
  • 【分类号】TE626.9
  • 【被引频次】4
  • 【下载频次】292
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