1990
DOI: 10.1016/0011-9164(90)80012-z
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Cross-Flow Microfiltration in the Food Industry. State of the Art

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Cited by 12 publications
(13 citation statements)
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“…It is, therefore, important to increase the transmembrane pressure stepwise to obtain optimum or critical flux region (Bacchin and others 2006). As time progress, the permeate flux declines mainly due to membrane fouling and other factors such as the morphology of the membrane together with fluid mechanics attributed to the flow of the feed across the membrane (Van Der Horst and Hanemaaijer 1990). …”
Section: Introductionmentioning
confidence: 99%
“…It is, therefore, important to increase the transmembrane pressure stepwise to obtain optimum or critical flux region (Bacchin and others 2006). As time progress, the permeate flux declines mainly due to membrane fouling and other factors such as the morphology of the membrane together with fluid mechanics attributed to the flow of the feed across the membrane (Van Der Horst and Hanemaaijer 1990). …”
Section: Introductionmentioning
confidence: 99%
“…MF membranes with a pore size of about 1.4 µm can achieve the right balance between rejection of bacteria and long‐term flux, with little or no rejection of other milk components such as protein, lactose and ash. Experimental results obtained under various operating conditions have been reported in a number of publications …”
Section: Cross‐flow Microfiltration For Bacteria Removal From Milkmentioning
confidence: 99%
“…2006). As time progresses, the permeate flux declines mainly due to membrane fouling and other factors (Van Der Horst and Hanemaaijer 1990) such as the change in morphology of the membrane and fluid mechanics created by flow of the LEW across the membrane.…”
Section: Introductionmentioning
confidence: 99%