文章摘要
石蜡基润滑油装置催化剂级配方案评价
Evaluation of Catalyst Grading Scheme for Paraffin Base Lubricating Oil Unit
投稿时间:2021-03-19  修订日期:2021-03-19
DOI:10.12136/j.issn.1000-890X.2022.07.0532
中文关键词: 润滑油基础油  减四线馏分油  加氢工艺  催化剂  馏分  收率
英文关键词: lubricating base oil  minus fourth-line distillate oil  hydrogenation process  catalyzer  fraction  yield
基金项目:
作者单位E-mail
徐岩峰* 中海油(青岛)重质油加工工程技术研究中心有限公司 xyf0523@126.com 
王启升 中海油气(泰州)石化有限公司  
张翠侦 中海油(青岛)重质油加工工程技术研究中心有限公司  
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中文摘要:
      采用中试装置,以石蜡基减四线馏分油为原料,评价两个催化剂级配方案生产高品质润滑油基础油的可行性。结果表明:采用三段高压加氢工艺的A催化剂级配方案,可得到满足Q/SY 44—2009指标要求的5cst及10cst润滑油基础油,在选定的试验条件下收率分别为17. 96%和45. 14%,280~360 ℃馏分无法满足2sct润滑油基础油的指标要求,但可作为变压器油基础油;采用三段加氢工艺的B催化剂级配方案,可得到满足指标要求的润滑油基础油,在选定的试验条件下2cst,5cst以及10cst润滑油基础油的收率分别为9. 01%,14. 56%和37. 17%。
英文摘要:
      The feasibility of producing high-quality lubricating base oil with two catalyst schemes was evaluated by using a pilot plant and minus fourth-line distillate oil as raw material.The results showed that,by using catalyst scheme A of three-stage high-pressure hydrogenation process,5cst and 10cst lubricating base oils which met the index requirements of Q/SY 44—2009 were obtained under the selected conditions,their yields were 17. 96% and 45. 14%,respectively,but the 280~360 ℃ fraction could not met the index requirements of 2sct lubricating base oil,and it could be used as the base oil for transformer oil.By using catalyst scheme B of three-stage hydrogenation process,the obtained lubricating base oils met the index requirements,and under the selected conditions,the yields of 2cst,5cst and 10cst lubricating base oil were 9. 01%,14. 56% and 37. 17%,respectively.
Author NameAffiliationE-mail
XU Yanfeng CNOOC(Qingdao) Heavy Oil Processing Engineering Research Center xyf0523@126.com 
WANG Qisheng CNOOC(Taizhou) Petrochemical Co.,Ltd  
ZHANG Cuizhen CNOOC(Qingdao) Heavy Oil Processing Engineering Research Center  
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