石油炼制与化工 ›› 2015, Vol. 46 ›› Issue (10): 72-76.

• 加工工艺 • 上一篇    下一篇

MIP技术及其专用剂在加氢重油催化裂化装置上的工业应用

朱渝   

  1. 中国石化上海石油化工股份有限公司
  • 收稿日期:2015-03-26 修回日期:2015-04-09 出版日期:2015-10-12 发布日期:2015-10-08
  • 通讯作者: 朱渝 E-mail:zhuy.shsh@sinopec.com

APPLICATION OF MIP TECHNOLOGY and PROPRIETARY CATALYSTS IN RFCC PROCESSING HYDROTREATED HEAVY OIL

  • Received:2015-03-26 Revised:2015-04-09 Online:2015-10-12 Published:2015-10-08

摘要: 介绍了MIP技术及其专用剂CRMI-2在上海石化3.5 Mt/a 重油催化裂化装置上的工业应用及标定情况。标定结果表明:采用MIP技术并使用专用催化剂CRMI-2,以加氢重油为主要原料且其性质略优于设计原料情况下,重油催化裂化装置的处理量超过设计值,同时装置产物分布优于设计值;主要表现为装置负荷率105.72%、110.11%时,汽油产率分别达到45.16%、46.89%,分别比设计值增加2.66和4.39百分点,而液体产品产率分别为81.36%、81.85%,比设计值分别增加了0.56和1.05百分点,焦炭产率明显低于设计值;稳定汽油中烯烃体积分数分别为24.4%、23.2%,均低于设计值,稳定汽油性质达到设计指标。

Abstract: The industrial application and calibration of MIP technology and its special catalyst CRMI-2 in 3.5Mt/a FCCU of SINOPEC Shanghai Petrochemical Company were introduced. The calibration results show that using MIP technology and special catalyst CRMI-2 and hydrotreated heavy oil feedstock, the process capacity of the unit exceeds its design value, and product yield distribution is better than design. Under the calibration conditions of maximum working load of 105.72% and 110.11%, the gasoline yields reach 45.16% and 46.89%, respectively, about 2.66 and 4.39 percentage points, higher than its design. The liquid product yields are 81.36% and 81.85%, respectively, about 0.56 percentage point and 1.05 percentage points, higher than the design value. The coke yield is significantly reduced. The olefin of stabilized gasoline is 24.4% and 23.2%, respectively, lower than its design value. The quality of the stabilized gasoline meets the design objective.