1994
DOI: 10.1002/aic.690401114
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Retention of proteins in cross‐flow UF through asymmetric inorganic membranes

Abstract: The flow and retention of 0.1 T o w/w aqueous solutions of pepsin, bovine serum albumin (BSA ), lipase, y-globulin, and invertase with molecular weights of 36,000, 67,000, 80,000, 150,000, and 270,000 dalton (g/mol)

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Cited by 26 publications
(10 citation statements)
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References 26 publications
(18 reference statements)
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“…Crossflow ultrafiltration is characterized by a rapid decline in permeate flux from the initial value. As mentioned in the literature [2,4,5], and also in this study, the steady state permeate flux is found to increase with increasing transmembrane pressure and velocity (see Figs. 2 and 3).…”
Section: Discussionsupporting
confidence: 86%
See 1 more Smart Citation
“…Crossflow ultrafiltration is characterized by a rapid decline in permeate flux from the initial value. As mentioned in the literature [2,4,5], and also in this study, the steady state permeate flux is found to increase with increasing transmembrane pressure and velocity (see Figs. 2 and 3).…”
Section: Discussionsupporting
confidence: 86%
“…Prµdanos et al [5] examined the flow and the retention coefficient of several proteins in the crossflow system through an inorganic microporous membrane with nominal pore size 0.02 · 10 -6 m. They analyzed the data within the frame of the film layer theory for the concentration polarization phenomenon. They obtained the mass transfer coefficient as a function of the feed circulation speed and the molecular weight of the protein.…”
Section: Introductionmentioning
confidence: 99%
“…is the use of the Film Theory of concentration polarization. This model is based on the use of the mass transfer coefficient, K m,i , in order to describe the solute transport in the membrane active layer (Kuhn et al, 2010;Prádanos et al, 1994) as…”
Section: Theorymentioning
confidence: 99%
“…One of the methods to do this consists in the use of the Film Theory of concentration polarization. 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 11 This model is based on the use of the mass transfer coefficient, K m,i , in order to describe the solute transport in the membrane active layer (Kuhn et al, 2010;Pradános et al, 1994) as…”
Section: Permeate Flux Decreasementioning
confidence: 99%