摘要
以炼油厂提供的重油催化裂化装置生产的催化汽油经过一段加氢脱硫得到的硫含量为35μg/g(0.0035%)的汽油为原料,进行萃取脱硫,最终确定:在以N,N-二甲基甲酰胺(DMF)为萃取剂,剂油比2.7∶1,萃取温度35℃,萃取级数为3,萃取30分钟时,硫含量由35μg/g降至9.8μg/g。
The sulfur content of the catalytic gasoline produced by the heavy oil catalytic cracking unit provided by the refinery is 35 μg/g (0.0035%) after a period of hydrodesulfurization as the raw material,and the desulfurization is carried out by extraction.Finally,when N,N-dimethyl formamide (DMF) was used as the extraction agent,the ratio of agent to oil was 2.7∶1,the extraction temperature was 35℃,the extraction order was 3,and the sulfur content decreased from 35 μg/g to 9.8 μg/g for 30 minutes.
作者
张伟伟
侯侠
李卫卫
齐晶晶
徐生杰
王建强
苏晓云
Zhang Weiwei;Hou Xia;Li Weiwei;Qi Jingjing;Xu Shengjie;Wang Jianqiang;Su Xiaoyun(Lanzhou Petrochemical College of Vocational Technology,Lanzhou 730060,China)
出处
《山东化工》
CAS
2019年第18期112-113,共2页
Shandong Chemical Industry
基金
甘肃省高等学校科研项目《加氢重汽油多级萃取脱硫探索研究》,课题编号:2018A-159
关键词
汽油
萃取
脱硫
gasoline
extraction
desulfurization
