Petroleum Refinery Engineering ›› 2021, Vol. 51 ›› Issue (12): 29-33.

• PROCESSING • Previous Articles     Next Articles

Effect of iron in feedstock on propylene production of heavy oil catalytic cracking unit

Guo Wei,Bai Rui,Yang Jinhua,Liu Hongwei,Bao Jicai,Liu Liqiang   

  1. SINOPEC Hainan Refining & Chemical Co., Ltd., Yangpu, Hainan 578101
  • Online:2021-12-15 Published:2021-12-17

原料中铁对重油催化裂化装置增产丙烯的影响分析

郭伟,白锐,杨进华,刘宏伟,鲍积才,刘丽强   

  1. 中国石化海南炼油化工有限公司,海南 洋浦 578101
  • 作者简介:郭伟,工程师,从事催化裂化装置的生产管理工作。E-mail:guow.hnlh@sinopec.com

Abstract: The RFCC unit of SINOPEC Hainan Refining & Chemical Co., Ltd. increases the production of propylene in LPG in the environment polluted by high content iron. The first stage is blank calibration stage, and the second stage adopts CMT catalyst system. The volume fraction of propylene in LPG increases by about 1.0% by recycling gasoline at different positions of riser. In the third stage, by changing the operating conditions and controlling the catalyst activity, the volume fraction of propylene in LPG increases by 3%~4% under the same amount of recycled gasoline, and the crude gasoline is finally refined and enters the lower nozzle of the riser. Combined with increasing the ratio of agent to oil in the device, the yield of propylene can reach more than 8%, achieving the purpose of decreasing oil and increasing chemical.

Key words: RFCC, propylene, iron content, iron resistant catalyst, recycling gasoline, increasing the ratio of agent to oil

摘要: 中国石化海南炼油化工有限公司重油催化裂化装置在原料铁含量高的环境下增产液化石油气、丙烯。第一阶段为空白标定阶段。第二阶段采用CMT催化剂体系,在相同操作条件下,通过在提升管不同位置回炼汽油,液化石油气中丙烯体积分数增长约1.0百分点。在第三阶段,通过改变操作条件、控制催化剂活性,在相同汽油回炼量下,液化石油气中的丙烯体积分数增长3~4百分点,最终得到回炼粗汽油,且进入提升管靠下的喷嘴,结合增加装置剂油比,丙烯收率可达8%以上,达到降油增化目的。

关键词: 重油催化裂化装置, 丙烯, 铁含量, 抗铁性催化剂, 回炼汽油, 增加剂油比