2006
DOI: 10.1016/j.ces.2006.01.049
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Prediction of pressure drop in a modified gas–liquid downflow bubble column

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Cited by 12 publications
(8 citation statements)
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References 27 publications
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“…As can be seen, the gas phase holdup was proportional to the gas suction rate. These are similar to the results related to gas phase holdup and suction rate in previous studies on vertical flow ejectors [2,5,6,[8][9][10][11][12][13][14][15].…”
Section: Gas Phase Holdupsupporting
confidence: 92%
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“…As can be seen, the gas phase holdup was proportional to the gas suction rate. These are similar to the results related to gas phase holdup and suction rate in previous studies on vertical flow ejectors [2,5,6,[8][9][10][11][12][13][14][15].…”
Section: Gas Phase Holdupsupporting
confidence: 92%
“…The gas phase holdup increased with increasing viscosity and surface tension of the liquid, whereas the mass-transfer coefficient in the ejector decreased with increasing viscosity by 60%, maximally [7]. In the vertical flow ejectors of the liquid-gas system, the correlation equations of the gas phase holdup with gas suction rate were found in previous studies [2,5,6,[8][9][10][11][12][13][14][15].…”
Section: Introductionmentioning
confidence: 59%
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“…To design and control such equipment efficiently, the values of pressure drops and volumetric fractions of phases must be determined (Begovich and Watson, 1978;Kato et al, 1981;Muroyama and Fan, 1985;Fan, 1989;Shah et al, 1982). Few experimental data on two-phase flow have been available in the downflow column (Marchese et al, 1992;Mandal et al, 2004;Majumder et al, 2006Majumder et al, , 2007Majumder et al, , 2010Sivaiah et al, 2010). There is a lack of studies on the phase fraction and pressure drops in this downflow system with gas-liquid-solid system.…”
Section: Introductionmentioning
confidence: 98%