| 气液氯化反应填料塔的设计模型 |
| |
| 引用本文： | 姚日生,邓胜松,尤亚华,张洪斌. 气液氯化反应填料塔的设计模型[J]. 化学工程, 2004, 32(3): 13-15,23 |
| |
| 作者姓名： | 姚日生 邓胜松 尤亚华 张洪斌 |
| |
| 作者单位： | 合肥工业大学,化工学院,安徽,合肥,230009;合肥工业大学,化工学院,安徽,合肥,230009;合肥工业大学,化工学院,安徽,合肥,230009;合肥工业大学,化工学院,安徽,合肥,230009 |
| |
| 基金项目： | 安徽省自然科学基金资助项目(99045420) |
| |
| 摘 要： | 将短湿壁管中的液膜面积和气体所通过的有效通道体积分别视作填料塔内有效传质面积和空隙体积,从短湿壁管测得的氯气与丙酮反应的气相传质关联式导出全新的且较为可靠的气液氯化反应填料塔的设计模型。其计算值与实际运行结果的最大相对误差仅为3.56%。
|
| 关 键 词： | 填料塔 设计模型 气液氯化反应 |
| 文章编号： | 1005-9954(2004)03-0013-03 |
Mathematic model of packed column for acetone/chlorine chlorination |
| |
| YAO Risheng,DENG Shengsong,YOU Yahua,ZHANG Hongbin. Mathematic model of packed column for acetone/chlorine chlorination[J]. Chemical Engineering, 2004, 32(3): 13-15,23 |
| |
| Authors: | YAO Risheng DENG Shengsong YOU Yahua ZHANG Hongbin |
| |
| Abstract: | The interface area of gas liquid phase and the channel space of gas in the short wetted wall tube were supposed to be equal to the effective area for the gas liquid mass transfer and the channel volume of the gas phase in the packed column respectively. On the basis of chlorine/acetone reaction mass transfer correlation was derived. Experiments proved the model sufficiently accurate in designing large scale packed column for chlorine/acetone chlorination, with the maximum relative error 3.56% between the theoretical and the actual value. |
| |
| Keywords: | packed column mathematic model gas-liquid chlorination |
| 本文献已被 CNKI 维普 万方数据 等数据库收录！ |
|
