摘要
介绍了偏三甲苯异构化生产均三甲苯生产现状,阐述了进行偏三甲苯异构化法生产均三甲苯装置的工业化改造的必要性,并对改造实施后的生产结果进行了分析,均三甲苯的生产成本下降了23%,均三甲苯生产能力达1 200 t/a。探讨了进一步提高均三甲苯装置经济效益的途径。
The production status of mesitylene were reviewed. The necessity of industrialized improvement of mesity-lene produced by 1,2,4-trimethylbenzene isomerization and how to make industrialized improvement were described . The production results were analyzed after the improvement. The production cost of mesitylene was reduced about 23 % , and production ability of mesitylene plant was up to 1 200 t/a. The way how to improve economic profits of mesitylene plant were discussed.
出处
《精细石油化工进展》
CAS
2004年第2期49-52,共4页
Advances in Fine Petrochemicals
关键词
异构化法
均三甲苯
抗氧剂
精馏系统
微放热反应
温度
mesitylene,1,2,4-trimethylbenzene, reaction system, rectification system, plant improvement