2015
DOI: 10.1002/aic.14967
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Nanocolloid cake properties determined from step‐up pressure filtration with single‐stage reduction in filtration area

Abstract: A sophisticated method was developed for evaluating simultaneously and accurately both the average specific resistance and average porosity of the filter cake formed in unstirred dead-end ultrafiltration of nanocolloids such as protein solution and nanosilica sol. In the method, a step-up pressure filtration test was conducted by using a filter with a singlestage reduction in the effective filtration area. The influence of the pressure drop across the cake on not only the average specific cake resistance but a… Show more

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Cited by 13 publications
(4 citation statements)
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References 59 publications
(75 reference statements)
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“…The specific resistance α av,i can be advantageously represented by an empirical correlation similar to Eq. in the form : true αnormalavnormal,normali = α1 (1- n1 )( Δ pc pa,1 ) (1+ Δ pnormalc pnormalanormal,1 )1- n1 -1 …”
Section: Theorymentioning
confidence: 99%
See 1 more Smart Citation
“…The specific resistance α av,i can be advantageously represented by an empirical correlation similar to Eq. in the form : true αnormalavnormal,normali = α1 (1- n1 )( Δ pc pa,1 ) (1+ Δ pnormalc pnormalanormal,1 )1- n1 -1 …”
Section: Theorymentioning
confidence: 99%
“…The C‐P data were successfully obtained with high accuracy by using the thus‐determined ε av . The method has been improved over the years , , and at present the pressure dependence of α av and ε av can be accurately determined from the flux decline behavior in step‐up pressure filtration by using a filter with a single‐stage reduction in the effective filtration area .…”
Section: Introductionmentioning
confidence: 99%
“…By assuming that the resistance of the filter medium is negligible, and the porosity of the cake is constant, the filtration theory can be linearized so that the permeability of the cake can be evaluated using linear fitting of the test data, that is, the linear plot of t/V versus V at a constant filtration pressure, where t and V are the filtration time and the volume of the filtrate respectively. The associated testing technique chiefly involves a filtration cell of constant pressure (Tien et al 2001), of stepped pressure (Murase 1989;Tarleton 2004;, or with the functionalities of sudden reduction in the filtration area (Murase et al 1987;Iritani et al 2015). Since the assumptions leading to the linearized theory are valid only for the latter part of the filtration test, the data obtained from the initial part of the test, that is, the gradual variation of the effective pressure drop across the cake with the time, are wasted.…”
Section: Introductionmentioning
confidence: 99%
“…As the most severe membrane fouling occurs in the dead-end mode, it is desirable to examine dead-end microfiltration behaviors in detail to clarify the role of the filter cake. Recently, several dead-end mode filtration tests have been proposed to accurately and simply determine the cake characteristics [ 8 , 20 , 21 , 22 , 23 , 24 , 25 , 26 ]. Among the cake characteristics, both the average specific cake resistance and average cake porosity, being related to the filterability, are recognized as the most important factors controlling membrane filtration behaviors.…”
Section: Introductionmentioning
confidence: 99%