Extractive Desulfurization from Simulated Sulfur-Rich Naphtha  

作　　者：Shen Xizhou Li Zhiqiang Fang Liuya Song Hao Gan Feng Shen Zhi 

机构地区：[1]Lab of Petroleum Refining, Wuhan Institute of Technology

出　　处：《China Petroleum Processing & Petrochemical Technology》2019年第3期61-67,共7页中国炼油与石油化工（英文版）

摘　　要：Upon extractive desulfurization of sulfur-rich oil obtained after recycling raffinate,the effects of single and compound extractants,temperature,and extractant/oil ratio on desulfurization rate,oil loss rate,extractant loss rate,and selectivity coefficient were investigated.The results showed that the thiophene existing in the simulated sulfur-rich oil could be further removed by extraction.The single-stage desulfurization rates achieved by dimethyl sulfoxide(DMSO)and sulfolane(SF)were 53.51%and 47.36%,respectively,while the selectivity coefficient of SF was 1.13,which was higher than that of DMSO(with a selectivity coefficient of 1.04).For the compound extractant,a single-stage desulfurization rate of 49.59%and a selectivity coefficient of 1.40 were obtained by using DMSO+10%MEA as the extractant,which was higher than that of SF.Upon using 50%SF+50%DMSO as the extractant,the single-stage desulfurization rate reached 50.92%with a selectivity coefficient of 1.32.Based on the comprehensive consideration,the DMSO+10%MEA extractant was selected as the best extractant for treating the sulfur-rich oil.Upon extractive desulfurization of sulfur-rich oil obtained after recycling raffinate, the effects of single and compound extractants, temperature, and extractant/oil ratio on desulfurization rate, oil loss rate, extractant loss rate, and selectivity coefficient were investigated. The results showed that the thiophene existing in the simulated sulfur-rich oil could be further removed by extraction. The single-stage desulfurization rates achieved by dimethyl sulfoxide(DMSO) and sulfolane(SF) were 53.51% and 47.36%, respectively, while the selectivity coefficient of SF was 1.13, which was higher than that of DMSO(with a selectivity coefficient of 1.04). For the compound extractant, a single-stage desulfurization rate of 49.59%and a selectivity coefficient of 1.40 were obtained by using DMSO+10%MEA as the extractant, which was higher than that of SF. Upon using 50%SF+50%DMSO as the extractant, the single-stage desulfurization rate reached 50.92% with a selectivity coefficient of 1.32. Based on the comprehensive consideration, the DMSO + 10% MEA extractant was selected as the best extractant for treating the sulfur-rich oil.

关 键 词：extractive DESULFURIZATION SIMULATED sulfur-rich oil dimethyl SULFOXIDE MONOETHANOLAMINE 

分 类 号：TE[石油与天然气工程]