2013
DOI: 10.1016/j.memsci.2012.09.032
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Intensification of microfiltration using a blade-type turbulence promoter

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Cited by 28 publications
(19 citation statements)
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“…However, membrane fouling during the process is one of the major disadvantages of this technology (4). Different techniques might be employed to reduce the membrane fouling: increase of crossflow velocity (5), promotion of turbulence (6,7,8,9,10), pulsation, backflushing (11), temperature increase (12), changes in pH (13), flocculation (14,15), and coagulation (16) of the suspension, introduction of external electrical field (17,18), and surface modification with temperature sensitive polymers (19). Membrane fouling becomes even more critical in crossflow microfiltration of disrupted cells as there are solids and solutes of various sizes, hydrophobicities, charge densities, solubilities, shapes, sensitivities to share force, etc.…”
Section: Please Scroll Down For Articlementioning
confidence: 99%
“…However, membrane fouling during the process is one of the major disadvantages of this technology (4). Different techniques might be employed to reduce the membrane fouling: increase of crossflow velocity (5), promotion of turbulence (6,7,8,9,10), pulsation, backflushing (11), temperature increase (12), changes in pH (13), flocculation (14,15), and coagulation (16) of the suspension, introduction of external electrical field (17,18), and surface modification with temperature sensitive polymers (19). Membrane fouling becomes even more critical in crossflow microfiltration of disrupted cells as there are solids and solutes of various sizes, hydrophobicities, charge densities, solubilities, shapes, sensitivities to share force, etc.…”
Section: Please Scroll Down For Articlementioning
confidence: 99%
“…The effect of turbulence promoter's geometry on the flow field in the membrane channel and fouling minimization have been widely presented. [4][5][6] Turbulence promoters of diverse geometries are studied in the microfiltration of various mixtures such as yeast, 7,8 skimmed milk, 4,6 bentonite, 9 etc. where excellent flux improvements were gained.…”
Section: Introductionmentioning
confidence: 99%
“…In addition, higher cross-flow velocities increase the wall shear rate at the membrane surface [12]. To further enlarge the benefit of inserts in the flow channel, their geometry is designed to induce secondary flows which enhance mixing and particle back transport into the bulk fluid [4,19]. For instance, wires are wound around a rod to establish a helical flow path forming vortices and flow instabilities [7,20].…”
Section: Introductionmentioning
confidence: 99%
“…This was explained by the change in flow path induced by the varying cross-section of the cone-shaped insert [25]. 6 kW h/m 3 , whereas less than 4.4 kW h/m 3 were necessary in the system with blade-type mixers [19]. However, the specific energy consumption was even lower when twisted tape mixers were applied instead of blade-type mixers [19].…”
Section: Introductionmentioning
confidence: 99%
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