A model for pressure drop and liquid saturation in gas–liquid cocurrent upflow through packed beds
Author:
Publisher
Elsevier BV
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,Environmental Chemistry,General Chemistry
Reference10 articles.
1. Flow regime identification and pressure drop in cocurrent gas–liquid upflow through packed beds;Khan;Bioprocess Eng.,1997
2. An analysis of the phase holdup in concurrent gas liquid upflow through packed beds using (I) drift-flux model, and (II) slip ratio;Khan;Bioprocess Eng.,2000
3. Liquid saturation in cocurrent upflow fixed-bed reactors: a state-of-the-art correlation;Bensetiti;Chem. Eng. Sci.,1997
4. Some experimental liquid saturation results in fixed bed reactors operated under elevated pressure in cocurrent upflow and downflow of the gas and the liquid;Larachi;Ind. Eng. Chem. Res.,1991
5. Hydrodynamics of two-phase concurrent downflow through packed beds;Rao;AIChE J.,1983
Cited by 4 articles. 订阅此论文施引文献 订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献
1. Pressure Drop in Concurrent Gas–Liquid Upflow Through Packed Beds;Lecture Notes in Mechanical Engineering;2024
2. Effects of internals on phase holdup and backmixing in a slightly-expanded-bed reactor with gas–liquid concurrent upflow;Chinese Journal of Chemical Engineering;2019-10
3. Pressure drop and its reduction of gas–non-Newtonian liquid flow in downflow trickle bed reactor (DTBR);Chemical Engineering Research and Design;2014-01
4. Prediction of pressure drop in liquid–liquid pulsed packed extraction countercurrent columns;International Journal of Heat and Fluid Flow;2013-12
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