石油炼制与化工 ›› 2015, Vol. 46 ›› Issue (11): 30-34.

• 加工工艺 • 上一篇    下一篇

MIP工艺在吉林石化1.40 Mt/a催化裂化装置的工业应用

王哲,赵权利,徐品德   

  1. 中国石油吉林石化分公司
  • 收稿日期:2015-04-03 修回日期:2015-07-09 出版日期:2015-11-12 发布日期:2015-10-27
  • 通讯作者: 王哲 E-mail:congli.cheng@outlook.com;jh_wz002@petrochina.com.cn

APPLICATION OF MIP TECHNOLOGY IN 1.40 Mt/a FCCU OF JILIN PETROCHEMICAL CORPORATION

  • Received:2015-04-03 Revised:2015-07-09 Online:2015-11-12 Published:2015-10-27

摘要: 多产异构烷烃的催化裂化工艺(MIP)是中国石化石油化工科学研究院开发的具有生产清洁汽油组分的技术。中国石油吉林石化分公司1.40 Mt/a催化裂化装置按MIP工艺要求进行改造,于2010年11月6日进行了工业运转,该装置一直保持平稳运转,操作难度与FCC工艺相当。标定结果表明:与现有的催化裂化工艺相比,MIP工艺优化了产物分布,表现在干气和油浆产率下降,液体收率增加;而且所生产的汽油烯烃含量下降,表明MIP技术具有良好的降低汽油烯烃含量的能力;汽油RON达到93.0,柴油十六烷值达到23,总液体收率达到81.15%,取得了较好的工业应用效果。

Abstract: The MIP process for maximizing iso-paraffins developed by Research Institute of Petroleum Processing,SINOPEC is a proprietary technology to produce clean gasoline component. The FCC-Ⅲ unit with 1.40 Mt/a in Jilin Petrochemical Corporation was revamped for MIP operation, and put into running smoothly since Nov.6,2010. The industrial results show that the adopted MIP process, in comparison with the previous conventional FCC process, the product slate with lower yields of dry gas and slurry, and a higher yield of total liquid products are obtained. The product gasoline is characterized by lower contents of olefin and sulfur. The RON of the gasoline is 93.0. The cetane number of the diesel product reaches 24. The total liquid yield (LPG+Gasoline+Diesel) is 81.15%.