Abstract:A comprehensive study has been made on the rates of liquid weeping from sieve trays in a hydraulic simulator.Results are reported both for air-water and air-Isopar M. A wide range of tray geometries and flow rates was used. The influence on the weep rate of individual parameters such as hole gas velocity, liquid rate, weir height, hole diameter, and fractional perforation area is discussed. The results have been correlated by expressing the weep flux as a function of the Froude number.
“…Lockett and Banik [16] have studied weeping in 3.2, 6.4, and 12.7 mm perforation plates in a large rectangular column (1.22 m 0.63 m). The free area was in the range of 10.2 to 15 %.…”
“…Lockett and Banik [16] have studied weeping in 3.2, 6.4, and 12.7 mm perforation plates in a large rectangular column (1.22 m 0.63 m). The free area was in the range of 10.2 to 15 %.…”
“…For sieve plates with large holes, Koziol and Koch [38] deduced a semiempirical correlation, making it possible to calculate the weeping factor for the water-air system. A correlation valid for this system was presented by Lockett and Banik [39] in 1986. The effect of preasure on liquid weeping was recently investigated by Priestman and Brown [40].…”
Section: Literature Review On the Phenomena Of Liquid Entrainment Andmentioning
The most important investigations on liquid weeping and entrainment in plate columns with downcomers are reviewed. The formulae for calculating column plate efficiency under conditions of liquid weeping and entrainment have been derived on the basis of mass balance equations. The presented model is a generalization of the models of AIChE and Colburn. Sample results are shown graphically. The effect of liquid entrainment on tray efficiency predicted by the model is in agreement with experimental data of F N .
“…The height of the separator baffle is crucial for determining the liquid wept from the two halves of the tray. To prevent any effect on the gas distribution, the height of the separator baffle must be lower than that of the chimney caps, and it must prevent any overflowing between the two sides [33,34]. The comparison between the experimental data and numerical predictions was limited to the relatively restricted set of available computational power and experimental data in the literature.…”
The weeping phenomenon was investigated using some experimental tests and a numerical model. The tests were performed within a 1.22‐m‐diameter pilot‐scale column including two chimney trays and two Nye test trays with an air‐water system. The rates of weeping were measured in the Nye trays with two heights of the weir and a hole area of 5 %. Moreover, the weeping rates in the outlet and inlet halves of the Nye tray and the total weeping rate were calculated. In the next step, an Eulerian‐Eulerian computational fluid dynamics (CFD) technique was used. The results show good agreement between the attained CFD findings and the experimental data.
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