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| 醋酸甲酯水解催化精馏过程的模拟计算 | |
| 引用本文： | 吴燕翔,谭天恩,王良恩,赵之山.醋酸甲酯水解催化精馏过程的模拟计算[J].过程工程学报,2000,21(1):24-29. |
| 作者姓名： | 吴燕翔 谭天恩 王良恩 赵之山 |
| 作者单位： | 1. 浙江大学化工系,杭州310013;福州大学化工系,福州350002 2. 浙江大学化工系,杭州310013 3. 福州大学化工系,福州350002 |
| 基金项目： | 福建省自然科学基金，天津大学校科研和教改项目，B97008，，， |
| 摘 要： | 采用非平衡级速率模型对醋酸甲酯水解的催化精馏中试过程进行了模拟计算,考察了回流进料比、进料水酯比和酯进料位置等的变化对醋酸甲酯水解率的影响, 不仅证实了中试实验所得的结论,还获得了难以通过实验取得的结果. |
| 关 键 词： | 醋酸甲酯 水解 催化精馏 模拟计算 |
| 修稿时间： | 1999-03-29 |
Simulation of the Catalytic Distillation Process for Hydrolysis of Methyl Acetate |
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| WU Yan-xiang,TAN Tian-en,WANG Liang-en,ZHAO Zhi-shan.Simulation of the Catalytic Distillation Process for Hydrolysis of Methyl Acetate[J].Chinese Journal of Process Engineering,2000,21(1):24-29. | |
| Authors: | WU Yan-xiang TAN Tian-en WANG Liang-en ZHAO Zhi-shan |
| Abstract: | The modified rate-based model is applied to simulate the pilot catalytic distillationprocess of methyl acetate hydrolysis. The influences of the ratio of reflux to feed, the mole ratioof water to methyl acetate in feed and the feeding position of methyl acetate on conversion ofmethyl acetate are examined. The agreement of calculated results with the pilot experimentaldata is satisfactory. Some important conclusions which are difficult to obtain from experimentalreseaxch are drawn from numerical simulation of the hydrolysis process. |
| Keywords: | methyl acetate hydrolysis catalytic distillation simulation |
| 本文献已被 CNKI 万方数据 等数据库收录！ | |