نمایش مختصر رکورد

dc.contributor.authorKeshavarz Alamdari, Eskandaren_US
dc.contributor.authorHaghshenas, D. F.en_US
dc.contributor.authorDarvishi, D.en_US
dc.contributor.authorSadrnezhaad, S.K.en_US
dc.date.accessioned1399-07-09T08:08:52Zfa_IR
dc.date.accessioned2020-09-30T08:08:52Z
dc.date.available1399-07-09T08:08:52Zfa_IR
dc.date.available2020-09-30T08:08:52Z
dc.date.issued2011-07-01en_US
dc.date.issued1390-04-10fa_IR
dc.identifier.citationKeshavarz Alamdari, Eskandar, Haghshenas, D. F., Darvishi, D., Sadrnezhaad, S.K.. (2011). Extraction of Zn, Mn and Co from Zn-Mn-Co-Cd-Ni containing solution using D2EHPA, CYANEX® 272 and CYANEX® 302. International Journal of Engineering, 24(2), 181-190.en_US
dc.identifier.issn1025-2495
dc.identifier.issn1735-9244
dc.identifier.urihttp://www.ije.ir/article_71909.html
dc.identifier.urihttps://iranjournals.nlai.ir/handle/123456789/335868
dc.description.abstractEffects of pH, D2EHPA, Cyanex® 302 and Cyanex® 272 on extractions of zinc, manganese and cobalt from a Zn-Mn-Co-Cd-Ni containing solution was comprehensively investigated at the room temperature. The addition of Cyanex® 302 indicated a left-shifting-effect on the extraction curve of zinc, a right-shifting-effect on the extraction curve of manganese and no effect on the extraction of cobalt. The addition of Cyanex® 272 shifted all three curves to the right. The most suitable extractant for separation of zinc from manganese was therefore 0.3–0.3 mixture of D2EHPA with Cyanex® 302 and for separation of manganese from cobalt was sole D2EHPA. The stoichiometric coefficient for the extraction reaction of zinc (whether using pure D2EHPA or a mixture made of D2EHPA with Cyanex® 272 or Cyanex® 302) was 3. It varied from 4 to 5 for manganese, when the quantity of Cyanex® 302 dissolved in D2EHPA increased from 0 to 100%. Utilizing the above results, a two stage leaching was devised to recover zinc, manganese and cobalt from a complex solution. At the first stage, a 0.6M D2EHPA extractant could recover zinc and a scrubbing reaction with organic:aqueous (O:A) ratio of 20:1 could wash-out cadmium from the raffinate. In the second stage, the leaching residue was treated with 0.6M D2EHPA for recovery of manganese. This stage was then followed by a one-stage scrubbing of cobalt with O:A ratio of 20:1.en_US
dc.format.extent146
dc.format.mimetypeapplication/pdf
dc.languageEnglish
dc.language.isoen_US
dc.publisherMaterials and Energy Research Centeren_US
dc.relation.ispartofInternational Journal of Engineeringen_US
dc.subjectSolvent extractionen_US
dc.subjectD2EHPAen_US
dc.subjectCYANEX® 272en_US
dc.subjectCYANEX® 302en_US
dc.subjectStoichiometric Coefficienten_US
dc.subjectOrganic Aqueous Solutionen_US
dc.titleExtraction of Zn, Mn and Co from Zn-Mn-Co-Cd-Ni containing solution using D2EHPA, CYANEX® 272 and CYANEX® 302en_US
dc.typeTexten_US
dc.contributor.departmentNew Materials, MERCen_US
dc.contributor.departmentMMPE, Amirkabir University of Technologyen_US
dc.contributor.departmentNM, MERCen_US
dc.contributor.departmentMaterials Science and Engineering, Sharif University of Technologyen_US
dc.citation.volume24
dc.citation.issue2
dc.citation.spage181
dc.citation.epage190
nlai.contributor.orcid0000-0003-2631-5863


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