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Ultrafiltration of lignin from black liquor: Modelling decline in flux

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dc.contributor.author Kekana, Petrus T
dc.contributor.author Sithole, Bishop B
dc.contributor.author Ramjugernath, D
dc.date.accessioned 2019-09-25T07:23:01Z
dc.date.available 2019-09-25T07:23:01Z
dc.date.issued 2019-02
dc.identifier.citation Kekana, P.T., Sithole, B.B. & Ramjugernath, D. 2019. Ultrafiltration of lignin from black liquor: Modelling decline in flux. Journal of Scientific and Industrial Research, vol 78, pp. 91-95 en_US
dc.identifier.issn 0022-4456
dc.identifier.issn 0975-1084
dc.identifier.uri nopr.niscair.res.in/bitstream/123456789/45765/1/JSIR%2078%282%29%2091-95.pdf
dc.identifier.uri http://nopr.niscair.res.in/handle/123456789/45765
dc.identifier.uri http://hdl.handle.net/10204/11129
dc.description Copyright: 2019 NISCAIR en_US
dc.description.abstract Ultrafiltration of black liquor was studied in three different modules, namely, radial cross flow, rectangular cross flow and stirred cell over a wide range of operating conditions. Effects of different cut-off membranes on the permeate flux and observed rejection were also studied in the stirred cell module. Effects of operating conditions, e.g. pressure difference, Reynolds number and feed concentration on the permeate flux and observed rejection were also investigated. Such comparative study may be useful to select a suitable module, membrane and a set of optimum operating conditions to achieve a desired quantity and quality of permeate flux. A comparative analysis of flux decline for different modules is also presented using a simple resistance-in-series model. en_US
dc.language.iso en en_US
dc.publisher NISCAIR en_US
dc.relation.ispartofseries Workflow;22638
dc.subject Black Liquor en_US
dc.subject Flux decline en_US
dc.subject Fouling en_US
dc.subject Lignin Ultrafiltration en_US
dc.title Ultrafiltration of lignin from black liquor: Modelling decline in flux en_US
dc.type Article en_US
dc.identifier.apacitation Kekana, P. T., Sithole, B. B., & Ramjugernath, D. (2019). Ultrafiltration of lignin from black liquor: Modelling decline in flux. http://hdl.handle.net/10204/11129 en_ZA
dc.identifier.chicagocitation Kekana, Petrus T, Bishop B Sithole, and D Ramjugernath "Ultrafiltration of lignin from black liquor: Modelling decline in flux." (2019) http://hdl.handle.net/10204/11129 en_ZA
dc.identifier.vancouvercitation Kekana PT, Sithole BB, Ramjugernath D. Ultrafiltration of lignin from black liquor: Modelling decline in flux. 2019; http://hdl.handle.net/10204/11129. en_ZA
dc.identifier.ris TY - Article AU - Kekana, Petrus T AU - Sithole, Bishop B AU - Ramjugernath, D AB - Ultrafiltration of black liquor was studied in three different modules, namely, radial cross flow, rectangular cross flow and stirred cell over a wide range of operating conditions. Effects of different cut-off membranes on the permeate flux and observed rejection were also studied in the stirred cell module. Effects of operating conditions, e.g. pressure difference, Reynolds number and feed concentration on the permeate flux and observed rejection were also investigated. Such comparative study may be useful to select a suitable module, membrane and a set of optimum operating conditions to achieve a desired quantity and quality of permeate flux. A comparative analysis of flux decline for different modules is also presented using a simple resistance-in-series model. DA - 2019-02 DB - ResearchSpace DP - CSIR KW - Black Liquor KW - Flux decline KW - Fouling KW - Lignin Ultrafiltration LK - https://researchspace.csir.co.za PY - 2019 SM - 0022-4456 SM - 0975-1084 T1 - Ultrafiltration of lignin from black liquor: Modelling decline in flux TI - Ultrafiltration of lignin from black liquor: Modelling decline in flux UR - http://hdl.handle.net/10204/11129 ER - en_ZA


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