Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid

Copyright © 2016 Published by Elsevier B.V. All rights reserved. A synergistic solvent extraction (SSX) system consisting LIX 63 and Versatic 10, which are both commercially available, was selected to recover both Ga(III) and In(III) from synthetic sulfate leach solutions of zinc refinery cementatio...

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Main Authors: Sankum Nusen, Torranin Chairuangsri, Zhaowu Zhu, Chu Yong Cheng
Format: Journal
Published: 2018
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Online Access:https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84955304200&origin=inward
http://cmuir.cmu.ac.th/jspui/handle/6653943832/55758
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Institution: Chiang Mai University
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spelling th-cmuir.6653943832-557582018-09-05T03:05:01Z Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid Sankum Nusen Torranin Chairuangsri Zhaowu Zhu Chu Yong Cheng Engineering Materials Science Copyright © 2016 Published by Elsevier B.V. All rights reserved. A synergistic solvent extraction (SSX) system consisting LIX 63 and Versatic 10, which are both commercially available, was selected to recover both Ga(III) and In(III) from synthetic sulfate leach solutions of zinc refinery cementation residues in one circuit. With the optimum composition of the SSX system, 86% In(III) and 92% Ga(III) were extracted in a single contact at pH 3.0. The extraction and stripping kinetics of In(III) and Ga(III) were fast at 40 °C. In(III) and Ga(III) were stripped readily using solution with low acidity of 0.05 M H2SO4. Based on the McCabe-Thiele diagrams constructed, 4 stages of extraction at an A/O ratio of 1.2 and 3 stages of stripping at an O/A ratio of 5 are required for the extraction and stripping of both In(III) and Ga(III). The synergistic effect on In(III) extraction was significant while that on Ga(III), extraction was insignificant. A conceptual flowsheet is proposed including the SSX system consisting of reagents that are all commercially available and offers the advantages of recovering both In(III) and Ga(III) in one circuit and stripping with low acidity solutions. 2018-09-05T03:00:57Z 2018-09-05T03:00:57Z 2016-03-01 Journal 0304386X 2-s2.0-84955304200 10.1016/j.hydromet.2016.01.007 https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84955304200&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/55758
institution Chiang Mai University
building Chiang Mai University Library
country Thailand
collection CMU Intellectual Repository
topic Engineering
Materials Science
spellingShingle Engineering
Materials Science
Sankum Nusen
Torranin Chairuangsri
Zhaowu Zhu
Chu Yong Cheng
Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid
description Copyright © 2016 Published by Elsevier B.V. All rights reserved. A synergistic solvent extraction (SSX) system consisting LIX 63 and Versatic 10, which are both commercially available, was selected to recover both Ga(III) and In(III) from synthetic sulfate leach solutions of zinc refinery cementation residues in one circuit. With the optimum composition of the SSX system, 86% In(III) and 92% Ga(III) were extracted in a single contact at pH 3.0. The extraction and stripping kinetics of In(III) and Ga(III) were fast at 40 °C. In(III) and Ga(III) were stripped readily using solution with low acidity of 0.05 M H2SO4. Based on the McCabe-Thiele diagrams constructed, 4 stages of extraction at an A/O ratio of 1.2 and 3 stages of stripping at an O/A ratio of 5 are required for the extraction and stripping of both In(III) and Ga(III). The synergistic effect on In(III) extraction was significant while that on Ga(III), extraction was insignificant. A conceptual flowsheet is proposed including the SSX system consisting of reagents that are all commercially available and offers the advantages of recovering both In(III) and Ga(III) in one circuit and stripping with low acidity solutions.
format Journal
author Sankum Nusen
Torranin Chairuangsri
Zhaowu Zhu
Chu Yong Cheng
author_facet Sankum Nusen
Torranin Chairuangsri
Zhaowu Zhu
Chu Yong Cheng
author_sort Sankum Nusen
title Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid
title_short Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid
title_full Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid
title_fullStr Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid
title_full_unstemmed Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid
title_sort recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with lix 63 and versatic 10 acid
publishDate 2018
url https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84955304200&origin=inward
http://cmuir.cmu.ac.th/jspui/handle/6653943832/55758
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