摘要
探索了用环烷酸钴为催化剂,用空气直接氧化邻二甲苯制取邻甲基苯甲酸的过程及基本反应原理。试验为kg级工业模拟中试试验,反应为间歇式反应,原料邻二甲苯一次投料量为4.2kg,目的产物为邻甲基苯甲酸,单程收率可达47%,总收率可达62.36%。采用正交设计法试验,筛选出了工艺过程的最佳操作条件:温度130℃,压力0.3MPa,空气流量0.8m3/h,反应时间6h。
The process of liquid phase oxidation of o xylene by air to produce o methyl benzoic acid using cobalt naphthenate as catalyst has been investigated on a kilogram level industrial simulative medium scale unit.The reaction was intermittent.The yield per pass of o methyl benzoic acid is up to 47% with a total yield of up to 62 36%.The optimum operation conditions were found to be temperature 130℃,pressure 0 3MPa,air flow rate 0 8m 3/h,and reaction time 6h.
出处
《石油化工》
EI
CAS
CSCD
北大核心
1998年第2期82-85,共4页
Petrochemical Technology
关键词
邻甲基苯甲酸
空气液相氧化
邻二甲苯
o methyl benzoic acid,oxidation in liquid phase by air,cobalt naphthenate