石油化工应用2024,Vol.43Issue(2) :108-112.DOI:10.3969/j.issn.1673-5285.2024.02.022

加氢裂化装置处理催化柴油工业实践

Hydrocracking unit for treating catalytic diesel industry practice

管家伟
石油化工应用2024,Vol.43Issue(2) :108-112.DOI:10.3969/j.issn.1673-5285.2024.02.022

加氢裂化装置处理催化柴油工业实践

Hydrocracking unit for treating catalytic diesel industry practice

管家伟1
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作者信息

  • 1. 中国石油化工股份有限公司镇海炼化分公司,浙江宁波 315207
  • 折叠

摘要

为适应炼油行业油品结构调整的趋势,降低企业柴汽比,提高企业市场竞争力,某炼化企业尝试通过少量改造,利用中国石化(大连)石油化工研究院有限公司开发的催化柴油选择性加氢转化技术(FD2G),在高压蜡油加氢裂化装置加工高芳烃含量的劣质催化柴油.生产出硫含量<0.50 mg/kg,氮含量<0.5 mg/kg,研究法辛烷值在92.5以上的高辛烷值清洁汽油调和组分以及硫含量<10.00 mg/kg,十六烷值与原料催化柴油相比增加10个单位的清洁柴油调和组分.

Abstract

To adapt to the trend of oil product structure adjustment in the refining industry,reducing the diesel-to-gasoline ratio of the enterprise,and promoting enterprise competitive ness,the catalytic diesel selective hydrogenation conversion technology(FD2G)developed by SINOPEC Dalian Research Institute of Petroleum and Petrochemicals.This technology is ap-plied in the high-pressure gas oil hydrocracking unit to process low-quality catalytic diesel with high aromatic content.Producing high octane clean gasoline blending components with sulfur content<0.50 mg/kg,nitrogen content<0.5 mg/kg,and research octane number above 92.5,as well as clean diesel blending components with sulfur content less than 10.00 mg/kg and cetane number increased by 10 units compared to raw material catalytic diesel.

关键词

加氢裂化/装置改造/催化柴油/工业实践

Key words

hydrocracking/plant modification/catalytic diesel/industrial practice

引用本文复制引用

出版年

2024
石油化工应用
宁夏化工学会

石油化工应用

影响因子:0.276
ISSN:1673-5285
参考文献量7
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