2015
DOI: 10.1016/j.idairyj.2015.07.002
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Influence of process temperature and microfiltration pre-treatment on flux and fouling intensity during cross-flow ultrafiltration of sweet whey using ceramic membranes

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Cited by 29 publications
(13 citation statements)
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“…Steinhauer et al (2015) also reported that the pH levels above the isoelectric point of β‐Lg caused an increase in the amount of deprotonated form of sulfhydryl group (Prot‐S − ) as a result of thiol/disulfide reactions, so β‐Lg becomes more reactive and exhibits a higher fouling tendency due to increased protein‐membrane interactions. Similarly, Barukčić et al (2015) reported that since the β‐Lg has free thiol groups, the tendency of the β‐Lg to make intermolecular disulfide bonds increases and it becomes easier to chemically bind to the protein surface layer. In addition, it was reported that the reactivity of BSA increases rapidly above pH 6, while α‐La has a negligible effect on fouling at neutral pH levels (Metsämuuronen & Nyström, 2009).…”
Section: Resultsmentioning
confidence: 95%
“…Steinhauer et al (2015) also reported that the pH levels above the isoelectric point of β‐Lg caused an increase in the amount of deprotonated form of sulfhydryl group (Prot‐S − ) as a result of thiol/disulfide reactions, so β‐Lg becomes more reactive and exhibits a higher fouling tendency due to increased protein‐membrane interactions. Similarly, Barukčić et al (2015) reported that since the β‐Lg has free thiol groups, the tendency of the β‐Lg to make intermolecular disulfide bonds increases and it becomes easier to chemically bind to the protein surface layer. In addition, it was reported that the reactivity of BSA increases rapidly above pH 6, while α‐La has a negligible effect on fouling at neutral pH levels (Metsämuuronen & Nyström, 2009).…”
Section: Resultsmentioning
confidence: 95%
“…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%
“…The implementation of non-thermal methods in the production of whey beverages, overcomes the above-mentioned difficulties, and improves the properties of existing products. (15)(16)(17)(18).…”
Section: Functional Foods and Beveragesmentioning
confidence: 99%