石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (11): 33-37.

• 催化剂 • 上一篇    下一篇

石蜡基原料油加氢异构脱蜡制润滑油基础油催化剂的研制

孟祥彬,高善彬,孙发民,胡胜   

  1. 中国石油石油化工研究院大庆化工研究中心
  • 收稿日期:2014-04-11 修回日期:2014-05-27 出版日期:2014-11-12 发布日期:2014-10-28
  • 通讯作者: 孟祥彬 E-mail:mengxb459@petrochina.com.cn

DEVELOPMENT OF HYDROISOMERIZATION CATALYST FOR LUBE BASE OIL PRODUCTION FROM PARAFFINIC FEEDSTOCKS

  • Received:2014-04-11 Revised:2014-05-27 Online:2014-11-12 Published:2014-10-28

摘要: 以AEL分子筛为载体,制备出一种贵金属异构脱蜡催化剂;以n-C12为模型物,以大庆炼化加氢预精制后的650SN糠醛精制油为实际原料考察该催化剂的加氢异构化催化性能。试验结果表明,所制备的异构脱蜡催化剂对n-C12以及650SN糠醛精制油均具有良好的异构化活性和选择性,其性能优于国外同类参比剂,加工650SN糠醛精制油时,可高收率地生产出优质API Ⅲ类润滑油基础油,目标产品倾点为-21 ℃,比采用参比剂时低6 ℃,重质基础油收率为62.79%,比采用参比剂时高5.55百分点。

Abstract: A hydroisomerization catalyst was developed based on AEL zeolite. n-C12 and the hydrotreated 650SN furfural refined oil were used as feeds, respectively, to evaluate the hydroisomerization performance of the catalyst. The results show that the catalyst has better hydroisomerization activity and selectivity. When processing 650SN, the high quality group API III lube base oil is produced. The pour point of the base oil reaches -21℃, 6℃ lower than the reference catalyst, and heavy base oil yield reaches 62.79%, 5.55% higher than the reference one, which indicates that the hydroisomerization performance of the catalyst is better than the reference catalyst.