石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (12): 54-58.

• 加工工艺 • 上一篇    下一篇

加氢裂化装置加工焦化蜡油操作优化

陈国伟1,郑文刚2   

  1. 1. 中国石化广州分公司
      2. 中国石油化工股份有限公司炼油事业部
  • 收稿日期:2014-04-15 修回日期:2014-06-28 出版日期:2014-12-12 发布日期:2014-11-27
  • 通讯作者: 陈国伟 E-mail:chengw.gzsh@sinopec.com

OPERATION OPTIMIZATION FOR PROCESSING COKER GAS OIL IN HYDROCRACKING UNIT

  • Received:2014-04-15 Revised:2014-06-28 Online:2014-12-12 Published:2014-11-27

摘要: 为改善催化裂化汽油质量,提高经济效益,中国石化广州分公司进行了加氢裂化装置原料掺炼焦化蜡油试验研究,结果表明,掺炼焦化蜡油后,加氢裂化尾油BMCI增大,乙烯裂解炉运行周期缩短。为解决该问题,利用英国KBC公司开发的Petro-SIM软件,模拟出加氢裂化装置最佳操作工况,将加氢裂化装置反应器压力由12.98 MPa提高至13.31MPa、分馏塔切割温度由369 ℃调整为375 ℃。优化后,加氢裂化尾油BMCI由13.01降至11.03,乙烯裂解炉运行周期从28天延长至52天。

Abstract: In order to improve the quality of FCC gasoline and increase the economic profit,SINOPEC Guangzhou Company, tried the hydrocracking of feedstock blending with coker gas oil. The results indicated that when processing the blending feed, the tail oil BMCI was increased and ethylene cracking furnace operation cycle was shortened. To solve these problems, we used KBC's Petro-SIM software to optimize the operation conditions of the hydrocracking unit. The optimized conditions are: hydrogen partial pressure of 13.31 MPa and the cut-point of fractionation tower of 375 ℃. After optimization, the tail oil BMCI decreases from 13.01 to 11.03, the cracking furnace coke cleaning cycle extend from 28 days to 52 days.