2006
DOI: 10.1016/j.memsci.2005.12.063
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Gas-sparged ultrafiltration using horizontal and inclined tubular membranes—A CFD study

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Cited by 39 publications
(13 citation statements)
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“…During the two-phase flow process, instable bubbles and flows can disturb CP and sweep away fouling layer on membrane surface. 148,149 It can be used in various PDMPs, (MBRs, 150 MF, 151 UF, 152 NF, 153 and RO 154 ) and modules 155 (tubular module, flat channel, hollow-fiber module, and submerged membrane) (see Supporting Information, Figure S2). Recently, Wibisono et al 155 reviewed related studies and applications of two-phase flow.…”
Section: Industrial and Engineering Chemistry Researchmentioning
confidence: 99%
“…During the two-phase flow process, instable bubbles and flows can disturb CP and sweep away fouling layer on membrane surface. 148,149 It can be used in various PDMPs, (MBRs, 150 MF, 151 UF, 152 NF, 153 and RO 154 ) and modules 155 (tubular module, flat channel, hollow-fiber module, and submerged membrane) (see Supporting Information, Figure S2). Recently, Wibisono et al 155 reviewed related studies and applications of two-phase flow.…”
Section: Industrial and Engineering Chemistry Researchmentioning
confidence: 99%
“…For example, J crit was increased 69% (from 28.8 to 48.8 L/m 2 h) while gas injector factor was varied from The reason was probably that gas sparging was more effective in a system where flux decline was dominated by concentration polarization than that coupled with fouling [14]. In addition, for controlled gas sparged ultrafiltration process, it was found that gas flow rate required for substantial improvements in permeate flux was very small [28]. A relatively low gas flow already suc- cessfully limited concentration polarization, leaving less room for further enhancement by higher gas flow.…”
Section: Effect Of Gas Sparging and Crossflow Rate On Critical Flux Amentioning
confidence: 99%
“…Membrane orientation has also been found to influence the mixing zone and flow patterns. Experimental and CFD studies on horizontal and inclined membranes have found that the length of the mixing zone increased with increasing inclination from the horizontal to the vertical 54. Flow of liquid around bubbles in inclined systems has been found to make patterns different from the ones made in horizontal systems.…”
Section: Ultrafiltrationmentioning
confidence: 99%