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复合脱酸剂清洁高效脱除减二线馏分油中环烷酸

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采用一种复合脱酸剂对减二线馏分油进行脱酸及回收环烷酸。利用酸值测定、黏度测试和FTIR等方法考察了反应工艺条件对脱酸效果的影响。实验结果表明,适宜的脱酸工艺条件为:反应温度30℃,剂油体积比 0。50,反应时间 15 min,相分离温度 25℃,相分离时间 60 min,在此条件下,脱酸率达到 92。70%,精制油酸值降为 0。33 mg/g,满足了工业上设备耐腐蚀的要求(酸值小于 0。50 mg/g),环烷酸在该复合脱酸剂相和油相的表观分配比达到了 24。79。与一级萃取相比,达到酸值小于 0。50 mg/g的标准时,三级萃取比一级萃取脱酸剂用量减少了40%以上。回收的环烷酸副产物品质较好,酸值为177。03 mg/g,达到了石油酸一级品55号酸值标准。
Composite deacidifier for efficiently removing naphthenic acid from second vacuum side-stream oil
A composite deacidifier was used to deacidize and recover naphthenic acid from second vacuum side-stream oil.The acid value titration,viscosity test and FTIR methods were used to investigate the effect of reaction conditions on the deacidification.The experimental results show that the appropriate deacidification process conditions are as follows:reaction temperature of 30℃,volume ratio of agent to oil of 0.50,reaction time of 15 min,phase separation temperature of 25℃,and phase separation time of 60 min.Under these conditions,the deacidification rate reaches 92.70%,and the acid value of refined oil decreases to 0.33 mg/g.The corrosion resistance requirements of industrial equipment are met(acid value is less than 0.50 mg/g),and the apparent distribution ratio of naphthenic acid in the composite deacidifier phase and oil phase reaches 24.79.When the acid value is less than 0.50 mg/g,the amount of deacidifier in the three-stage extraction is more than 40%less than that in the first-stage extraction.It is found that the quality of the recovered naphthenic acid by-product is good,and the acid value is 177.03 mg/g,which reaches the acid value standard of No.55 of the first-grade petroleum acid.

second vacuum side-stream oilcomposite deacidifierextraction separationrecovery

赵强、汪鹏飞、杨帅康、张浩哲、乔英云、田原宇

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中国石油大学(华东)化学化工学院,山东 青岛 266580

中海石油宁波大榭石化有限公司,浙江 宁波 315000

减二线馏分油 复合脱酸剂 萃取分离 回收

2025

石油化工
中国石化集团资产经营管理有限公司 北京化工研究院 中国化工学会石油化工专业委员会

石油化工

北大核心
影响因子:0.916
ISSN:1000-8144
年,卷(期):2025.54(1)