石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (2): 68-73.

• 加工工艺 • 上一篇    下一篇

2.0 Mt/a全循环加氢裂化装置首次开工运行分析及操作优化

穆海涛,姚立松   

  1. 中国石化青岛炼油化工有限责任公司
  • 收稿日期:2013-04-16 修回日期:2013-05-11 出版日期:2014-02-12 发布日期:2014-01-17
  • 通讯作者: 穆海涛 E-mail:mht.qdlh@sinopec.com;mhtvrds@126.com

ANALYSIS OF START-UP AND OPERATION OF 2.0 Mt/a HYDROCRACKING UNIT WITH FULL CYCLE MODE

  • Received:2013-04-16 Revised:2013-05-11 Online:2014-02-12 Published:2014-01-17

摘要: 为解决柴油质量升级的问题,中国石化青岛炼油化工责任有限公司新建2.0 Mt/a加氢裂化装置,首次开工的标定结果表明,采用全循环方案,在精制温度367 ℃、裂化温度381 ℃的条件下,脱硫率为99.35%,轻油收率为94.30%。装置投入正常生产后,通过采取提高尾油循环量、降低精制反应深度、提高裂化反应深度等优化措施增产喷气燃料,喷气燃料收率达到36.55%。

Abstract: To upgrade the diesel, a new hydrocracking unit with 2.0 Mt/a capacity was built in Sinopec Qingdao Refining & Chemical Company. The caliberation for the start-up operation indicate the good performance of the catalyst system of FF36/3963/FC32, under the conditions of 367℃in refining stage, cracking temperature of 381℃ with full recycle mode,the sulfur removal rate is 99.35% with the light fraction yield of 94.30%. In the normal production, the jet fuel yield can reach 36.55% by mild refining、more severe cracking conditions and more amount of recycle tail oil.