## Abstract A method of estimating the true conditions of operation of a bubbleβcap tray is presented. Intermediate between the Murphree and the Lewis methods, which represent the extremes of actual operation, this method involves the use of a correlation to determine the degree of liquid mixing on
Efficiency in bubble cap distillation columns
β Scribed by C.T. Everitt; H.P. Hutchison
- Publisher
- Elsevier Science
- Year
- 1966
- Tongue
- English
- Weight
- 170 KB
- Volume
- 21
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
SEVERAL investigations have shown that the performance of a distillation column appears to be a function of composition [1, 2]. This variation in performance has been observed for many different systems and column types, and the reason would appear to be one which is general to the process of rectification rather than specific to any given circumstances. This communication is concerned with the variation in performanee for bubble cap columns.
The description of mass transfer on a bubble cap plate must necessarily be considerably simplified due to the complex fluid dynamics of such a device. If one assumes plug flow of vapour and a liquid which is well mixed vertically, then for an area of the tray where the liquid composition is uniform the basic rate equations can be integrated to give [3]
π SIMILAR VOLUMES
This Paper considers the behaviour of the distillation trays in conventional use in cryogenic air separation plants. An earlier study showed that the trays should operate at higher efficiencies than plant experience would indicate. This conclusion was based on the assumption of uniform liquid flow a