期刊文献+
共找到2篇文章
< 1 >
每页显示 20 50 100
Shortcut Procedure for Inverted Batch Distillation Column (I) Multicomponent Ideal System 被引量:12
1
作者 许松林 HectorE.Salomone oscara.iribarren 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2001年第1期28-33,共6页
Inverted batch distillation column(stripper) is opposed to a conventional batch distillation column(rectifier). It has a storage vessel at the top and products leave the column at the bottom. The batch stripper is fav... Inverted batch distillation column(stripper) is opposed to a conventional batch distillation column(rectifier). It has a storage vessel at the top and products leave the column at the bottom. The batch stripper is favourable to separate mixtures with a small amount of light components by removing the heavy components as bottom products. In this paper, we are presenting a shortcut procedure based on our earlier work for design and simulation of the inverted batch distillation column, which is equivalent to the Fenske-Underwood-Gilliland procedure for continuous distillation. Given a separation task, we propose to compute the minimum number of stages(Nbmin) and the minimum reboil ratio(Rbmin) required in a batch stripper,which are the stages and reboil ratio required in a hypothetical inverted batch distillation column operating in total reboil ratio or having an infinite number of stages,respectively. Then, it is shown that the performance of inverted batch columns with a finite number of stages and reboil ratios could be correlated in Gilliland coordinates with the minimum stages Nbmln and the minimum reboil ratio Rbmin. 展开更多
关键词 反置式间歇蒸馏塔 程序设计 多组分理想物质 汽提塔 化工设备
下载PDF
Operation of a Batch Stripping Distillation Column 被引量:7
2
作者 许松林 JoseEspinosa +1 位作者 HectorE.Salomone oscara.iribarren 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2001年第2期141-144,共4页
A stripping batch distillation column is preferred when the amount of the light component in the feed is small and the products are to be recovered at high purity. The operation modes of a batch stripping are believe... A stripping batch distillation column is preferred when the amount of the light component in the feed is small and the products are to be recovered at high purity. The operation modes of a batch stripping are believed to be the same as those of a rectifier. However, the control system of a stripper is different. In this paper, we explore three different control methods with Hysys (Hyprotech Ltd. 1997) for a batch stripper. The main difference is the control scheme for reboiler liquid level: (a) controlled by reflux flow; (b) controlled by reboiler heat duty; (c) controlled by bottom product flow. The main characteristics of operating a batch stripper with different control scheme are presented in this paper. Guidelines are provided for the startup of a batch stripper, the effects of somecontrol tuning parameters on the column performance are discussed. 展开更多
关键词 间歇提馏塔 操作体系 纯度 组分分离 回流
下载PDF
上一页 1 下一页 到第
使用帮助 返回顶部