石油炼制与化工

• 加工工艺 • 上一篇    下一篇

裂解乙烯副产C9馏分制备芳烃溶剂油及石油树脂

杨靖华 许修强 曹祖宾   

  1. 辽宁石油化工大学 辽宁石油化工大学石油化工学院
  • 收稿日期:2007-07-03 修回日期:1900-01-01 出版日期:2008-02-12 发布日期:2008-02-12
  • 通讯作者: 杨靖华

PREPARATION OF AROMATIC SOLVENT NAPHTHA BY C9 FRACTION FROM ETHYLENE CRACKING UNIT

  

  • Received:2007-07-03 Revised:1900-01-01 Online:2008-02-12 Published:2008-02-12

摘要: 利用沸程在100~200 ℃裂解乙烯的副产C9馏分为原料,研究了以Lewis酸为催化剂的两段聚合法制备芳烃溶剂油的工艺条件。主要考察催化剂用量、聚合温度、聚合时间对产品分布的影响。结果表明,采用两段聚合法,在催化剂三氟化硼乙醚络合质量分数1.0%、三氯化铝质量分数1.5%、聚合温度60℃、聚合时间6 h的条件下,芳烃溶剂油收率为71.1%,石油树脂收率最高可达20%;同时所得的芳烃溶剂油切割为120号和200号,指标达到行业标准。

关键词: C9馏分, 芳烃溶剂油, 120#溶剂油, 200#溶剂油, 石油树脂

Abstract: The preparation of aromatic solvent naphtha by two-stage polymerization over Lewis acid catalyst was studied using C9 fraction, the by-product of ethylene cracking unit, as feedstock. The effects of catalyst dosage, reaction temperature and reaction time on the product distributions were investigated. Results showed that under the conditions of a reaction temperature of 60℃, a reaction time of 6 h and a catalyst consisted of 1.0% BF3-ether and 1.5% AlCl3, the yields of aromatic solvent naphtha and petroleum resin reached 71.1% and 20%, respectively. The qualities of the obtained solvents (cut to 120# and 200#) could meet the requirements of trade standard SH0005-90.

Key words: C9 fraction, Aromatic solvent naphtha, 120# solvent naphtha, 200# solvent naphtha, Petroleum resin