2017
DOI: 10.4025/actascitechnol.v39i5.27585
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<b>Cake formation and the decreased performance of whey ultrafiltration

Abstract: Fouling in whey ultrafiltration is still a problem to be solved and modelling the permeate flux is still a challenge. A set of experiments of whey ultrafiltration was performed and it was demonstrated that the cake filtration model accurately represents the permeate flux over time despite exist more complex models to describe the phenomenon. In less than 10 s an irreversible resistance is established, and the cake starts to build up. It was observed changes in protein rejection in a range of 98 and 94% when a … Show more

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Cited by 12 publications
(3 citation statements)
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“…The C20F membrane had a sharp decrease in the beginning that transitioned into a pseudo steady state mode and ended with a profile that followed the RC70PP and C5F. The sharp decrease in the beginning was probably caused by the formation of a cake on the surface as seen and explained by Brião et al [28] and Hwang et al [29]. The C30F had a larger MWCO than the C20F: thus, it was expected to have an overall higher flux based on this and the higher PWF seen in Figure 5.…”
Section: Resultsmentioning
confidence: 76%
“…The C20F membrane had a sharp decrease in the beginning that transitioned into a pseudo steady state mode and ended with a profile that followed the RC70PP and C5F. The sharp decrease in the beginning was probably caused by the formation of a cake on the surface as seen and explained by Brião et al [28] and Hwang et al [29]. The C30F had a larger MWCO than the C20F: thus, it was expected to have an overall higher flux based on this and the higher PWF seen in Figure 5.…”
Section: Resultsmentioning
confidence: 76%
“…The pressures of 1.5 and 2.5 bar present different flux development, and consequently different forms of fouling. At the lowest pressure (1.5 bar), pore blockage occurs simultaneously with cake formation and at the highest pressure (2.5 bar) (Figure 3), pore blockage occurs at the first moment, causing a drastic reduction in permeate flux within initial minutes of UF, and after that a slow drop, by cake formation as the solutes are deposited on the membrane (Brião et al, 2017). The Ho and Zydney (2000) model (Equation ( 6)) fit experimental data better for 1.5 bar with R 2 = .9876 compared with 2.5 bar where R 2 = .9208.…”
Section: Resultsmentioning
confidence: 99%
“…In state of the art, the use of UF membranes concerning their pore size and surface charge for the fractionation of the dairy components is accepted as a promising process especially in the valorisation of whey protein. However, due to the presence of a large number of proteins such as bovine serum albumin, ᾰ- and ß-lactoglobulin in the dairy wastewater can limit the use of the UF membrane, which contributes towards the severe membrane fouling (Barukčić et al 2015 ; Brião et al 2017 ). In a recent study (Damar et al 2020 ), the whey protein recovery was investigated using different commercially available UF membranes with different characteristics.…”
Section: Protein Recovery By Membrane Technologymentioning
confidence: 99%