石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (1): 131-137.

• 加工工艺 • 上一篇    下一篇

催化裂解装置掺炼减压渣油的生产实践

赵长斌   

  1. 中海石油宁波大榭石化有限公司
  • 收稿日期:2024-03-18 修回日期:2024-06-07 出版日期:2025-01-12 发布日期:2024-12-27
  • 通讯作者: 赵长斌 E-mail:zhaochb@cnooc.com.cn

PRACTICE OF MIXING VACUUM RESIDUE INTO DEEP CATALYTIC CRACKING UNIT

  • Received:2024-03-18 Revised:2024-06-07 Online:2025-01-12 Published:2024-12-27

摘要: 某公司在2.2 Mt/a催化裂解(DCC)装置上进行了掺炼减压渣油(简称“减渣”)的生产实践。针对掺炼减渣后,混合原料性质变差对装置产品分布、产品性质、操作参数、催化剂剂耗、能耗以及长周期稳定运行的影响,进行了综合分析,并采取了相应的应对措施。结果表明:通过将上游装置原料改为中/轻质原油,改善了DCC装置掺炼减渣原料的品质;通过优化DCC装置掺炼比例,调整DCC装置操作参数,增加金属钝化剂加入量,加大催化剂置换量等一系列应对措施,削弱了原料残炭升高导致装置结焦倾向增大,以及Ni、Ca、Fe等重金属污染催化剂的不利影响,开创了同类装置掺炼减渣的先例,保证了装置安全平稳运行;当减渣掺炼比(w)达44.4%时,装置总液体收率降低1.61百分点,焦炭产率增加1.87百分点,能耗增加230.903 MJ/t。

关键词: 催化裂解, 减压渣油, 原料优化, 催化剂,

Abstract: A company has carried out the production practice of mixing vacuum residue(VR)into a 2.2 Mt/a deep catalytic cracking (DCC) unit. After mixing VR, the effect of mixed feed quality deterioration on product distribution, product properties, operating parameters, catalyst consumption, energy consumption and long-term stable operation of the plant was comprehensively analyzed, and corresponding countermeasures were taken. The results show that the raw material quality of DCC is improved by changing the raw material of upstream unit to medium/light crude oil. By optimizing the mixing ratio of DCC unit feed, adjusting the operating parameters of DCC unit, increasing the dosage of metal passivator,increasing the amount of catalyst replacement and other countermeasures, the increase of coking tendency of the unit caused by the increase of raw material carbon residue and the adverse effects of heavy metals such as Ni, Ca, Fe,and so on,were weakened, creating a precedent for the mixing VR of similar units,which can ensure the safe and smooth operation of the device. When the VR blending ratio (w) reached 44.4%, the total liquid yield decreased by 1.61 percentage points, the coke yield increased by 1.87 percentage points, and the energy consumption increased by 230.903 MJ/t.

Key words: deep catalytic cracking, vacuum residue, feedstock optimization, catalyst, calcium