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| 甲缩醛反应精馏过程模拟 | |
| 引用本文： | 秦娟妮,刘继泉. 甲缩醛反应精馏过程模拟[J]. 当代化工, 2007, 36(3): 285-287 |
| 作者姓名： | 秦娟妮 刘继泉 |
| 作者单位： | 青岛科技大学化工学院,山东,青岛,266042 |
| 摘 要： | 通过实验取得了甲醛和甲醇合成甲缩醛的反应参数;建立了其连续生产工艺的数学模型,利用ASPEN PLUS软件对甲醛和甲醇缩合生成甲缩醛进行了模拟,结果表明反应精馏连续生产甲缩醛的工艺是可行的,转化率高达99%,并得到含甲缩醛99%的产物,同时确定了进料板和反应区. |
| 关 键 词： | 反应精馏 甲缩醛 动力学 模拟 |
| 文章编号： | 1671-0460（2007）03-0285-03 |
| 修稿时间： | 2006-10-142006-10-19 |
Simulation of Methylal Eactive Distillation Process |
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| QIN Juan-ni,LIU Ji-quan. Simulation of Methylal Eactive Distillation Process[J]. Contemporary Chemical Industry, 2007, 36(3): 285-287 | |
| Authors: | QIN Juan-ni LIU Ji-quan |
| Abstract: | The experiment gains reaction parameters of methylal from formaldehyde and methanol,it also found a mathematical model for continuous production process.The synthesis of methylal using formaldehyde and methanol is simulated by ASPEN PLUS software.The results show that process produced methylal through reactive distillation and continuous production is feasible,in which convertion rate is promoted to 99 %,and obtain production contained 99 % methylal,feed and reaction tray are also determined. |
| Keywords: | reactive distillation methylal knitics simulation |
| 本文献已被 CNKI 维普 万方数据 等数据库收录！ | |