2014
DOI: 10.1002/ceat.201300837
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Effect of Structural Parameters on Drop Size Distribution in Pulsed Packed Columns

Abstract: The effect of packing type on drop size distribution in pulsed packed columns was investigated by means of different columns and three packing types with three liquid systems including n‐butyl acetate, toluene, and kerosene with water. These liquid systems cover a wide range of interfacial tensions. Also the influence of operating variables in terms of pulse intensity and volumetric flow rates of dispersed and continuous phases was examined. Pulse intensity, interfacial tension, and packing shape were found as… Show more

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Cited by 24 publications
(9 citation statements)
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“…Consequently, hold up will increase with higher rate. 14,26 The similar results have been reported for this extraction column by some authors. 15,27 The inuence of continuous phase supercial velocity on the hold-up is shown in Fig.…”
Section: Dispersed Phase Hold-upsupporting
confidence: 90%
See 1 more Smart Citation
“…Consequently, hold up will increase with higher rate. 14,26 The similar results have been reported for this extraction column by some authors. 15,27 The inuence of continuous phase supercial velocity on the hold-up is shown in Fig.…”
Section: Dispersed Phase Hold-upsupporting
confidence: 90%
“…Consequently, hold up will increase with higher rate 14,26 . The interfacial energy which is responsible for keeping drop surface is lower in low value of interfacial tension.…”
Section: Dispersed Phase Hold-upmentioning
confidence: 99%
“…The pulsed extraction columns are among the extractors that avoid frequent maintenance, making remote operation possible. Moreover, they are designed in packed, perforated-plate, and disc and doughnut forms [4][5][6]. In another classification, the pulsed extraction columns can be divided into two major categories: vertical columns and horizontal columns.…”
Section: Introductionmentioning
confidence: 99%
“…In addition, increasing the continuous phase flow rate acts as a barrier to the dispersed phase and does not release along the column. Therefore, the dispersed phase hold up is enhanced by increasing the continuous phase flow rate; however, the mean drop size is not significantly affected by the continuous phase . Hence, the interfacial area available for mass transfer is increased according to Equation .…”
Section: Resultsmentioning
confidence: 99%