石油炼制与化工 ›› 2017, Vol. 48 ›› Issue (9): 54-58.

• 加工工艺 • 上一篇    下一篇

增强型催化裂解装置开工初期调整策略及效果

赵长斌   

  1. 中海石油宁波大榭石化有限公司
  • 收稿日期:2017-03-31 修回日期:2017-04-27 出版日期:2017-09-12 发布日期:2017-08-25
  • 通讯作者: 赵长斌 E-mail:zhaocb8552@126.com
  • 基金资助:
     

PROBLEMS AT INITIAL STAGE OF DCC-PLUS UNIT, MEASURES ADJUSTMENT AND EFFECT

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  • Received:2017-03-31 Revised:2017-04-27 Online:2017-09-12 Published:2017-08-25
  • Contact: Zhao Changbin E-mail:zhaocb8552@126.com
  • Supported by:
     

摘要: 中海石油宁波大榭石化有限公司采用中国石化石油化工科学研究院开发的增强型催化裂解(DCC-plus)技术,新建1套2.2 Mt/a DCC-plus装置。针对开工初期,采用外购平衡剂开工,且原料油性质与设计原料存在差异,造成主要产品乙烯、丙烯收率与设计值相差较大的问题,在对影响乙烯、丙烯收率的主要因素进行分析的基础上,通过采取优化原料配比、工艺操作参数、催化剂配方等措施,使乙烯、丙烯收率分别达到了4.53%、19.52%,达到了设计值。由于DCC-plus装置的高乙烯收率,后续乙苯-苯乙烯等化工装置达到了满负荷操作,DCC-plus装置运行平稳。

关键词: DCC-plus, 乙烯, 丙烯, 优化

Abstract: A new 2200 kt/a unit adopting DCC-plus technology developed by Research Institute of Petroleum Processing SINOPEC, was set in CNOOC Ningbo Daxie Petrochemical Limited Company. There were some problems met at the initial stage of the unit: lower yields of ethylene and propylene than the design value due to the outsourcing e-cat for start-up and the feed qualities deviate from the design requirement. The ethylene and propylene yields are increased to 4.53w% and 19.52w%, respectively by means of optimizing operating parameters, ratio of feed composition and catalyst formula. These results meet the design requirements of DCC-plus unit and thus make the downstream ethylbenzene-styrene unit run at full capacity.

Key words: DCC-plus, ethylene, propylene, optimization

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