Evaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der Ryst

Using kerosene as an aromatic organic diluent in the liquid–liquid separation process for the extraction of uranium in the solvent extraction section of the AngloGold Ashanti South Uranium Plant near the town of Orkney in South Africa, incurs a multitude of safety, health and environmental problems....

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Main Author: Van der Ryst, Reinier Hendrik
Published: North-West University 2011
Online Access:http://hdl.handle.net/10394/4921
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spelling ndltd-netd.ac.za-oai-union.ndltd.org-nwu-oai-dspace.nwu.ac.za-10394-49212014-04-16T03:53:11ZEvaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der RystVan der Ryst, Reinier HendrikUsing kerosene as an aromatic organic diluent in the liquid–liquid separation process for the extraction of uranium in the solvent extraction section of the AngloGold Ashanti South Uranium Plant near the town of Orkney in South Africa, incurs a multitude of safety, health and environmental problems. A possible solution may be to replace the currently used aromatic–based organic diluent with an aliphatic–based organic diluent. A range of aliphatic organic diluents were tested to determine the extraction efficiency of these alternative diluents, if they were to be applied to the process currently implemented by the AngloGold Ashanti South Uranium Plant. The aliphatic organic diluents under investigation were: Biodiesel-B–100 Shellsol D70 Sasol Wax SSX 150 Sasol Wax SSX 210 The aliphatic diluent yielding the highest uranium extraction efficiency, and having the most desirable physical characteristics, was Sasol Wax SSX 210. Sasol Wax SSX 210 was selected to replace kerosene as the diluent in the solvent composition to conduct the next phase of the study. The solvent’s composition was then optimised to obtain a desirable solvent make–up containing the newly chosen aliphatic diluent, third–phase inhibitor and tertiary alkyl amine. The most favourable solvent composition was found to be; 5 vol.% Alamine 336 with 2 vol.% isodecanol and 93 vol.% SSX 210. A third parameter, pH, was identified as an influencing factor on the overall efficiency of the process. A theoretical explanation for the influence that pH has on the process, confirmed by an experimental analysis, was examined to determine which pH characteristics contributed to the efficiency of the extraction process. A final indication of the success of the newly implemented aliphatic solvent was determined via a precipitation simulation. The structure of crystals precipitated from the loaded strip liquor (OK liquor) was evaluated to ensure that the required product would adhere to product specifications.Thesis (M.Ing. (Chemical Engineering))--North-West University, Potchefstroom Campus, 2011.North-West University2011-10-05T10:43:44Z2011-10-05T10:43:44Z2010Thesishttp://hdl.handle.net/10394/4921
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sources NDLTD
description Using kerosene as an aromatic organic diluent in the liquid–liquid separation process for the extraction of uranium in the solvent extraction section of the AngloGold Ashanti South Uranium Plant near the town of Orkney in South Africa, incurs a multitude of safety, health and environmental problems. A possible solution may be to replace the currently used aromatic–based organic diluent with an aliphatic–based organic diluent. A range of aliphatic organic diluents were tested to determine the extraction efficiency of these alternative diluents, if they were to be applied to the process currently implemented by the AngloGold Ashanti South Uranium Plant. The aliphatic organic diluents under investigation were: Biodiesel-B–100 Shellsol D70 Sasol Wax SSX 150 Sasol Wax SSX 210 The aliphatic diluent yielding the highest uranium extraction efficiency, and having the most desirable physical characteristics, was Sasol Wax SSX 210. Sasol Wax SSX 210 was selected to replace kerosene as the diluent in the solvent composition to conduct the next phase of the study. The solvent’s composition was then optimised to obtain a desirable solvent make–up containing the newly chosen aliphatic diluent, third–phase inhibitor and tertiary alkyl amine. The most favourable solvent composition was found to be; 5 vol.% Alamine 336 with 2 vol.% isodecanol and 93 vol.% SSX 210. A third parameter, pH, was identified as an influencing factor on the overall efficiency of the process. A theoretical explanation for the influence that pH has on the process, confirmed by an experimental analysis, was examined to determine which pH characteristics contributed to the efficiency of the extraction process. A final indication of the success of the newly implemented aliphatic solvent was determined via a precipitation simulation. The structure of crystals precipitated from the loaded strip liquor (OK liquor) was evaluated to ensure that the required product would adhere to product specifications. === Thesis (M.Ing. (Chemical Engineering))--North-West University, Potchefstroom Campus, 2011.
author Van der Ryst, Reinier Hendrik
spellingShingle Van der Ryst, Reinier Hendrik
Evaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der Ryst
author_facet Van der Ryst, Reinier Hendrik
author_sort Van der Ryst, Reinier Hendrik
title Evaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der Ryst
title_short Evaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der Ryst
title_full Evaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der Ryst
title_fullStr Evaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der Ryst
title_full_unstemmed Evaluation of the solvent extraction organic phase in a uranium extraction plant / Reinier Hendrik van der Ryst
title_sort evaluation of the solvent extraction organic phase in a uranium extraction plant / reinier hendrik van der ryst
publisher North-West University
publishDate 2011
url http://hdl.handle.net/10394/4921
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