反置式高温动态选粉机的研制与应用

第三代选粉机在不同技术条件下,根据不同需要发展了多种类型,反置式高温动态选粉机是专为适应高温物料分选而开发的新型选粉机,由于具有独特的笼轮锥体反置结构,避免了主轴轴承受到高温环境的影响,在实际应用中取得了良好的效果。     

带多个中间贮罐的新型分批精馏塔的研究

多罐分批精馏塔由多个分批精馏塔依次连接而成,它只在第一个塔的塔釜加热,在最后一个塔的塔顶设冷凝器。采用恒摩尔持液模型对多贮罐的新型分批精馏塔的研究结果表明：多罐分批精馏塔具有可同时获得多个高纯度产品、无过渡馏分、产率高、操作简单及节能的特点。对多罐分批精馏塔和常规分批精馏塔进行出较的结果显示：采用多罐分批精馏塔分离产品可获得的年利润远高于采用常规分批精馏塔。     

轻型高效精馏塔的计算机辅助设计

论述了在Win9x操作环境下,用Visual Baisc 6.0可视化语言设计界面,用Microsoft Access建立数据库,用Auto CAD VBA编辑绘图程序,以Auto CAD作为平台,开发设计轻型高效精馏塔辅助设计软件。通过对实际设计结果的检验与试用,该软件具有良好的用户界面、人机对活功能和图形功能,使用简单方便,输入初始条件即可设计并绘制出塔结构图。     

Traitement par une méthode d'éléments finis de modèles de colonnes de rectification discontinue à garnissage

Mathematicals models representing several operating modes of a packed batch distillation column are detailed. In the first part, the authors consider steady-state operation with total reflux, where the axial and radial dispersion phenomena are superimposed on the plug flow of the liquid and vapour phases. The equations are solved by means of a finite element method based on the Galerkin criterion, and also by using a finite difference procedure. The numerical study of the steady-state operating mode, including both axial and radial dispersion phenomena, allows us to note that the last term can be, in most cases, neglected. On the other hand, the dynamic model analysis has shown that the axial dispersion phenomenon is always indispensable for accurately representing the column operation.     

多罐复合式分批精馏塔的设计

为了开发多罐复合塔简单易行的设计方法,建立了多罐复合塔的恒摩尔持液模型,并用平衡程度系数概念考察了全回流过程中塔内各板和各罐内接近平衡的情况,在综合考虑所需塔板数和操作时间的基础上提出了设计中确定全回流操作终点的方法,给出了多罐复合式分批精馏塔的设计方法,该方法确定的板数能较好地完成分离任务。     

带中间贮槽的间歇精馏塔的模拟计算

带中间贮槽的间歇精馏塔由２个分离段及其中间的贮槽组成。假定液体持液量和待分离的体系的相对挥发度均保持不变,建立了该塔的一个简化的模型,由此得到各组分在整个塔中的分布情况。在此基础上,又考察了各个操作参数对分离效果的影响。     

全回流-全馏出与变塔压联合的间歇精馏过程

A novel operation of batch distillation-combination of varying colum pressure and total reflux-total efflux is studied experimentally. In the operation, the product is accumulated at the top of the column under total reflux and then drained off completely, and the column pressure is varying in the whole process. This process has been industrialized successfully with large profits. The conventional mode of batch distillation is improved by this method effectively: the separation eficiency and the yield of product are increased greatly, the operation time is shortened and the production cost is cut down. Moreover, the amount of condensation water is decreased and the over-high reboiler temperature is lowered.     

香茅油间歇精馏塔的工艺计算

对300t/a香茅油间歇精馏塔进行物料衡算,根据物料衡算的结果对精馏塔的操作温度、最小理论板数、理论板数、最小回流比、操作回流比和塔径等进行计算,获得塔体的工艺和设备参数。     

间歇精馏新型操作方式的研究进展

本文综述了国内外近年来间歇精馏新型操作方式的研究进展和发展方向,重点介绍了塔顶累积全回流操作、反向间歇精馏塔操作、中间贮罐以及多罐间歇精馏塔操作,阐述了这些新型毛主席匠特点及应用前景。     

间歇提馏塔的操作

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 some control tuning parameters on the column performance are discussed.