Abstract

Parallel-flow trays incorporating slotted sieve tray decks were originally developed for air separation applications. They are still used for that purpose and also in a wide range of chemical and petrochemical separations. The present paper outlines the main features of the trays, including the liquid flow-path arrangement and the slotting pattern that is typically used. The results of an experimental study are presented in which the tray efficiency was measured by using a 6.1 m diameter air-water tray simulator. The system used was acetone stripped from water by air. This is a convenient system because the slope of the equilibrium line is close to unity and so the results are relevant to distillation systems. For purposes of comparison, trays were tested both with and without a slotted tray deck. In the latter case, severe liquid maldistribution was evident. The measured tray efficiencies of the slotted and unslotted trays were found to be similar when no outlet weirs were used, but the slotted tray had a lower froth height and pressure drop. Theory was used to predict the point efficiencies for the two trays and to show that the slotted tray had a larger enhancement of tray efficiency over point efficiency than the unslotted tray. The measured tray efficiencies divided by the calculated point efficiencies were compared with theoretical predictions and reasonable agreement was demonstrated.

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.