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dc.contributor.authorMakaka, Siphokazi
dc.date.accessioned2014-03-06T08:58:57Z
dc.date.accessioned2016-01-27T10:14:24Z
dc.date.available2014-03-06T08:58:57Z
dc.date.available2016-01-27T10:14:24Z
dc.date.issued2011
dc.identifier.urihttp://hdl.handle.net/20.500.11838/866
dc.descriptionThesis submitted in fulfilment of the requirements for the degree Master of Technology: Chemical Engineering in the Faculty of Engineering at the Cape Peninsula University of Technology 2011en_US
dc.description.abstractTreatment of waste material from mining and mineral processing is gaining increasing importance as a result of the increasing demand for high purity products and environmental concerns. Supported liquid membranes (SLMs) have been proposed as a new technology for the selective removal of metal ions from a solution. This technology can be described as the simultaneous extraction and stripping operation, combined in a continuous single process unit. Theoretically, the rate of mass transfer through SLM systems could be controlled by three resistances, namely: · Resistance through the feed-side · Resistance through the strip-side laminar layers; and · Diffusion through the membrane. It has been reported that transport resistance in the feed-side laminar layer is controlling. (Srisurichan et al, 2005:186). The objective of this research was to extract copper ions in a TSLM system, evaluate the effect of the feed characteristics on the feed-side laminar layer and determine a relationship between the applicable dimensionless numbers, i.e. Sherwood, Schmidt and Reynolds numbers. A Counter-current, double pipe Perspex bench-scale reactor, consisting of a single hydrophobic PVDF tubular membrane mounted vertically within, was used for the test work. The membrane was impregnated with LIX 984N-C and became the support for this organic transport medium. Dilute Copper solution passed through the centre pipe and sulphuric acid, as a strippant, passed through the shell side. In this test work, Copper was successfully transported from the feed-side to the strip-side and through repetitive results; a relationship between dimensionless numbers was achieved.en_US
dc.language.isoenen_US
dc.publisherCape Peninsula University of Technologyen
dc.rights.urihttp://creativecommons.org/licenses/by-nc-sa/3.0/za/
dc.subjectMass transfer -- Chemical engineeringen_US
dc.subjectSolvent extraction -- Chemical engineeringen_US
dc.subjectLiquid membranesen_US
dc.subjectMembrane processes -- Chemical engineeringen_US
dc.subjectCopper -- Metallurgyen_US
dc.subjectDissertations, Academicen_US
dc.subjectMTechen_US
dc.subjectTheses, dissertations, etc.en_US
dc.titleThe development of an empirical mass transfer relationship for the extraction of copper ions in a carrier facilitated tubular supported liquid membrane systemen_US
dc.typeThesisen_US


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