石油炼制与化工 ›› 2026, Vol. 57 ›› Issue (9): 10-16.

• 加工工艺 • 上一篇    下一篇

高硫高金属渣油生产低硫低钒石油焦S-COKE技术开发与国内首次工业应用

戴立顺1,孙永福2,胡大为1,田晨2,刘涛1,徐维敬2,施瑢1,李金力2,王振1,李泽池2,董明1   

  1. 1. 中石化石油化工科学研究院有限公司
    2. 河北冠宇化工有限公司
  • 收稿日期:2025-04-22 修回日期:2026-03-19 出版日期:2026-09-12 发布日期:2026-08-21
  • 通讯作者: 施瑢 E-mail:shirong.ripp@sinopec.com
  • 基金资助:
    中国石化联合会科技指导计划项目

DEVELOPMENT OF S-COKE TECHNOLOGY FOR PRODUCING LOW SULFUR AND LOW VANADIUM PETROLEUM COKE FROM HIGH SULFUR AND HIGH METAL RESIDUE AND ITS FIRST COMMERCIAL APPLICATION IN CHINA


  • Received:2025-04-22 Revised:2026-03-19 Online:2026-09-12 Published:2026-08-21

摘要: 针对国内炼化企业普遍存在的高硫石油焦问题,中石化石油化工科学研究院有限公司开发了S-COKE技术,即焦化原料加氢预处理与延迟焦化组合工艺。该技术以劣质高硫高钒渣油为原料,旨在低成本生产硫质量分数小于3.0%、钒质量分数小于300 μg/g的低硫低钒石油焦,同时提高液体产品收率。基础研究结果表明,通过适度提高反应温度、大幅提高空速,可在相同脱硫率下降低氢耗;稀释油种类及比例对脱金属效果有显著影响。该技术在某公司2.60 Mt/a渣油加氢装置及配套延迟焦化装置上实现国内首次工业应用。结果表明,装置实际加工原料金属(镍+钒)质量分数高达200 μg/g左右,通过优化催化剂级配方案(增加脱金属剂比例)和反应温度操作模式(前部反应器提温、后部反应器控温),第二周期氢耗显著降低,运行周期延长至近1年。延迟焦化装置单炼加氢减压渣油后,石油焦硫质量分数降至1.84%、钒质量分数降至250 μg/g,达到低硫低钒石油焦要求;液体产品收率提高13.04百分点,焦炭产率降低11.43百分点。

关键词: 渣油加氢, 延迟焦化, 石油焦, 硫, 钒

Abstract: To address the problem of high-sulfur petroleum coke in domestic refining and chemical enterprises, SINOPEC Research Institute of Petroleum Processing Co., Ltd. has developed the S-COKE technology, which is a combined process of residue hydrotreating and delayed coking. This technology utilizes inferior high-sulfur, high-vanadium residue as feedstock, aiming to produce low-sulfur, low-vanadium petroleum coke with a sulfur mass fraction of less than 3.0% and a vanadium mass fraction of less than 300 μg/g at low cost, while increasing the yield of liquid products. Fundamental research shows that by moderately increasing the reaction temperature and significantly raising the volume space velocity, hydrogen consumption can be reduced at the same desulfurization rate; the type and proportion of diluent oil have a significant effect on demetallization performance. This technology achieved its first commercial application in China on a 2.60 Mt/a residue hydrotreating unit and its supporting delayed coking unit at a company. The results show that the actual feedstock processed in the unit had a metal (nickel+vanadium) mass fraction as high as about 200 μg/g. By optimizing the catalyst grading (increasing the proportion of demetallization catalyst) and the reaction temperature operation mode (raising temperature in the front reactors and controlling temperature in the rear reactors), the hydrogen consumption in the second cycle was significantly reduced, and the operating cycle was extended to about one year. After the delayed coking unit processed only the hydrotreated residue, the sulfur mass fraction of the petroleum coke dropped to 1.84% and the vanadium mass fraction to 250 μg/g, meeting the low-sulfur, low-vanadium standard; the yield of liquid products increased by 13.04 percentage points, while the coke yield decreased by 11.43 percentage points.

Key words: residue hydrotreating, delayed coking, petroleum coke, sulfur, vanadium