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高标6#溶剂油生产装置工艺改造
引用本文:刘元直,徐政雄,杜红换,孟令华. 高标6#溶剂油生产装置工艺改造[J]. 现代化工, 2005, 25(3): 56-57
作者姓名:刘元直  徐政雄  杜红换  孟令华
作者单位:中国石化中原油气高新股份有限公司天然气处理厂,河南,濮阳,457162
摘    要:针对以油田稳定轻烃为原料生产父了改进,改造方案由"双塔流程改三塔流程"及"加氢精制流程"2部分组成.新工艺提高了6#溶剂油中正己烷的含量及其与芳烃的分离精度,经过加氢精制的高标6#溶剂油中芳烃质量分数降至0.005%以下.介绍了新工艺的创新点,并对技术改进后的经济效益进行了相应分析.

关 键 词:溶剂油  精馏  芳烃  加氢  工艺改造
文章编号:0253-4320(2005)03-0056-02
修稿时间:2004-11-23

Technical modification of production process of high quality solvent oil 6#
LIU Yuan-zhi,XU Zheng-xiong,DU Hong-huan,MENG Ling-Hua. Technical modification of production process of high quality solvent oil 6#[J]. Modern Chemical Industry, 2005, 25(3): 56-57
Authors:LIU Yuan-zhi  XU Zheng-xiong  DU Hong-huan  MENG Ling-Hua
Abstract:Based on the problems existing in the traditional production process of high quality solvent oil 6~# from stable light hydrocarbon in oil fields,the modification is carried out,which includes 2 parts,i.e. changing the process from 2 rectifying towers into 3 towers with the hydrofining process of aromatics added in solvent oil 6~#.The content of hexane in solvent oil 6~# and the separation precision are improved,and the mass fraction of aromatics in hydrofined solvent oil 6~# is decreased below 0.005%.The innovative characteristics of the new process were introduced,and the economic results was also analyzed.
Keywords:solvent oil  refinery  aromatics  hydrogenation  technical modification
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