Please use this identifier to cite or link to this item: http://nopr.niscair.res.in/handle/123456789/45765
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dc.contributor.authorKekana, P T-
dc.contributor.authorSithole, B B-
dc.contributor.authorRamjugernath, D-
dc.date.accessioned2019-02-07T06:54:25Z-
dc.date.available2019-02-07T06:54:25Z-
dc.date.issued2019-02-
dc.identifier.issn0975-1084 (Online); 0022-4456 (Print)-
dc.identifier.urihttp://nopr.niscair.res.in/handle/123456789/45765-
dc.description91-95en_US
dc.description.abstractFundamental studies on membrane fouling caused by organic matter during ultrafiltration have been carried out widely by using the stirred dead-end filtration setup. In this study, black liquor ultrafiltration experiments have been carried out using a hydrophilic polyethersulfone membrane with a cut-off size of 10kDa in a stirred batch cell over a wide range of operating conditions. The effect of operating conditions (pressure, feed concentration and stirring rate) on transient flux profiles was studied in order to elucidate the fouling mechanism involved. Results indicated that the operating conditions have a significant effect on the flux decline behaviour. The solute mass balance for a stirred cell and the intermediate blocking model were applied to model the flux decline experimental data. The simulation results were compared to the experimental results and they were found to be in good agreement predominantly for filtration time that was ≥ 20 minutes.en_US
dc.language.isoen_USen_US
dc.publisherNISCAIR-CSIR, Indiaen_US
dc.rights CC Attribution-Noncommercial-No Derivative Works 2.5 Indiaen_US
dc.sourceJSIR Vol.78(02) [February 2019]en_US
dc.subjectFlux Declineen_US
dc.subjectMembraneen_US
dc.subjectFoulingen_US
dc.subjectModellingen_US
dc.subjectUltrafiltrationen_US
dc.titleUltrafiltration of Lignin from Black Liquor: Modelling Decline in Fluxen_US
dc.typeArticleen_US
Appears in Collections:JSIR Vol.78(02) [February 2019]

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