| 连续法生产乙二醇醋酸酯 |
| |
| 引用本文： | 范存良,杨忠保,奚军.连续法生产乙二醇醋酸酯[J].精细石油化工进展,2001,2(11):39-41. |
| |
| 作者姓名： | 范存良 杨忠保 奚军 |
| |
| 作者单位： | 1. 上海石油化工股份有限公司化工研究所
2. 上海石油化工股份有限公司化工研究所, |
| |
| 摘 要： | 在带静态混合器的反应器中进行乙二醇醋酸酯的生产，对反应器内的温度分布进行了优化，环氧乙烷与醋酸的较佳摩尔比为1．05∶1．0，有机碱性化合物作催化剂时，反应的选择性大于95％。物料在反应器内的停留时间越长，反应的转化率和选择性越好。
|
| 关 键 词： | 乙二醇醋酸酯 醋酸 环氧乙烷 反应器 连续法 |
| 修稿时间： | 2001年10月17 |
Continuous Production of Ethylene Glycol Acetate |
| |
| Fan Cunliang Yang Zhongbao Xi Jun.Continuous Production of Ethylene Glycol Acetate[J].Advances in Fine Petrochemicals,2001,2(11):39-41. |
| |
| Authors: | Fan Cunliang Yang Zhongbao Xi Jun |
| |
| Abstract: | Ethylene glycol acetate was manufactured in a tubular reactor with static mixer. The better ratio of ethy-lene oxide to acetic acid was 1.05:1.0, the distribution of temperature inside the reactor was optimized. The selec-tivity of the reaction was up to 95 % in the presence of organic alkaline compound as a catalyst. The longer the re-tention time of reactant in reactor was, the higher the yield and selectivity could be obtained. |
| |
| Keywords: | ethylene glycol acetate acetic acid ethylene oxide reactor |
| 本文献已被 CNKI 维普 万方数据 等数据库收录！ |
