石油炼制与化工 ›› 2022, Vol. 53 ›› Issue (7): 1-5.

• 加工工艺 •    下一篇

DCC工艺技术灵活性及其在化工型炼油厂的应用

谢朝钢   

  1. 中国石化石油化工科学研究院
  • 收稿日期:2021-11-19 修回日期:2021-12-21 出版日期:2022-07-12 发布日期:2022-06-29
  • 通讯作者: 谢朝钢 E-mail:xiecg.ripp@sinopec.com

FLEXIBILITY OF DCC TECHNOLOGY AND ITS COMMERCIAL APPLICATION IN CHEMICAL-TYPE REFINERY

  • Received:2021-11-19 Revised:2021-12-21 Online:2022-07-12 Published:2022-06-29

摘要: 对催化裂解(DCC)和增强型催化裂解(DCC-plus)技术的特点以及两者的关系进行了简述,DCC-plus技术比DCC具有更高的丙烯产率,同时干气和焦炭产率明显减少。对于1套加工50%常压渣油与50%加氢裂化尾油混合原料的2.2 Mt/a DCC-plus装置,其乙烯和丙烯产率分别达到5.6%和21.5%。对1套1.2 Mt/a DCC-plus装置进行了油品方案和烯烃方案两种生产模式的切换操作,与油品方案相比,按烯烃方案操作时丙烯产率增加125.8%,裂解石脑油和裂解轻油产率分别减少37.4%和20.0%。DCC技术成熟可靠,装置大型化和长周期运转都已得到工业验证。对于以DCC装置为核心的化工型炼油流程,油品率(汽油、柴油和喷气燃料的总产量占原油加工量的比例)可以低至16.0%,而化学品率(丙烯、芳烃和乙烯原料的总产量占原油加工量的比例)高达67.3%,成为构建新一代全化工型炼油厂具有竞争力的技术选择。

关键词: 催化裂解, 原料适应性, 操作灵活性, 大型化, 长周期, 工业验证

Abstract: The characteristics of deep catalytic cracking (DCC) and enhanced deep catalytic cracking (DCC-plus) technology and their relationships were reviewed. DCC-plus technology has higher propylene yield than DCC technology, and the yield of dry gas and coke is significantly reduced. For a set of 2.2 Mt/a DCC-plus unit for processing 50% atmospheric residue mixed with 50% hydrocracking tail oil as feedstock, the yields of ethylene and propylene yields were 5.6% and 21.5%, respectively. A set of 1.2 Mt/a DCC-plus unit has switched between two operation modes of fuel oil program and olefins program. Compared with the fuel oil mode, the propylene yield was increased by 125.8%, and the DCC naphtha and light cycle oil (LCO) yields were reduced by 37.4% and 20.0%,respectively,under the olefins production mode. DCC technology is mature and reliable, and the large-scale and long-term operation of DCC unit has been verified in industry. For chemical refineries with the DCC units as the core, the oil product ratio (the total output of gasoline, diesel and aviation fuels as a proportion of crude oil processing) can be as low as 16.0%, and the rate of chemicals (the total production of propylene, aromatics and ethylene as a proportion of crude oil processing) is as high as 67.3%, which is a competitive technical choice for building a new generation of full chemical-type refinery.

Key words: deep catalytic cracking, feedstock adaptability, operation flexibility, large scale, long term, commercial verification