Comparison of sequential and simultaneous draining in periodic cycled separation columns

Jess Rasmussen, Seyed Mansouri, Jens Abildskov, Jakob Huusom*

*Corresponding author for this work

Research output: Contribution to conferenceConference abstract for conferenceResearchpeer-review

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Abstract

Periodic (or cyclic) distillation is an intensified distillation process first proposed in the 1960’s [1], where the liquid and the vapor phase flows are divided in two separate periods [2,3]. The two periods are a vapor flow period (VFP) and a liquid flow period (LFP). During the VFP, the liquid holdup(s) on the trays are in fixed positions, while vapor flows through the column. During the LFP, the liquid is drained from one tray to the tray below, followed by a new VFP and so forth. By operating a distillation in cyclic mode, the separation efficiency has been shown to be higher than for conventional distillation [3]. When replacing a conventional distillation column with a cyclic distillation column, a smaller column with fewer trays is needed for the same separation [1]. Depending upon the design, energy consumption may also be reduced. This expands the range of options for designs [2,3].
The theory of cyclic distillation was developed during the 20th century. However, industrial applications are only slowly coming along [3]. A serious problem with the first generation of realizations was the need for improved liquid flow control. This problem was solved in different ways during the 1980s. In recent years, new trays [4] have made it possible to operate any size column in periodic mode and thus making cyclic distillation feasible in large scale. With this tray design there is still an issue regarding the need for interrupting the vapor flow during LFPs. This can cause significant pressure dynamics. An alternative tray design has been developed that implies draining of the trays occur sequentially instead of simultaneously [5].
The currently available models are relatively simple. These models are often based on mass balances and neglect effects of pressure drop, energy transfer and variations of the point efficiency. Furthermore, it is only the more recent models that allows multi-component mixtures and non-linear phase equilibrium. In addition to this, (nearly) all existing models address simultaneous draining, which means there is a need for models that describes the sequential draining for comparison.
Original languageEnglish
Publication date2019
Number of pages2
Publication statusPublished - 2019
EventECCE12, the 12th European Congress of Chemical Engineering -
Duration: 15 Sep 201919 Sep 2019

Conference

ConferenceECCE12, the 12th European Congress of Chemical Engineering
Period15/09/201919/09/2019

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