| dc.contributor.author | Keshavarz Alamdari, Eskandar | en_US |
| dc.contributor.author | Haghshenas, D. F. | en_US |
| dc.contributor.author | Darvishi, D. | en_US |
| dc.contributor.author | Sadrnezhaad, S.K. | en_US |
| dc.date.accessioned | 1399-07-09T08:08:52Z | fa_IR |
| dc.date.accessioned | 2020-09-30T08:08:52Z | |
| dc.date.available | 1399-07-09T08:08:52Z | fa_IR |
| dc.date.available | 2020-09-30T08:08:52Z | |
| dc.date.issued | 2011-07-01 | en_US |
| dc.date.issued | 1390-04-10 | fa_IR |
| dc.identifier.citation | Keshavarz 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.issn | 1025-2495 | |
| dc.identifier.issn | 1735-9244 | |
| dc.identifier.uri | http://www.ije.ir/article_71909.html | |
| dc.identifier.uri | https://iranjournals.nlai.ir/handle/123456789/335868 | |
| dc.description.abstract | Effects 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.extent | 146 | |
| dc.format.mimetype | application/pdf | |
| dc.language | English | |
| dc.language.iso | en_US | |
| dc.publisher | Materials and Energy Research Center | en_US |
| dc.relation.ispartof | International Journal of Engineering | en_US |
| dc.subject | Solvent extraction | en_US |
| dc.subject | D2EHPA | en_US |
| dc.subject | CYANEX® 272 | en_US |
| dc.subject | CYANEX® 302 | en_US |
| dc.subject | Stoichiometric Coefficient | en_US |
| dc.subject | Organic Aqueous Solution | en_US |
| dc.title | Extraction of Zn, Mn and Co from Zn-Mn-Co-Cd-Ni containing solution using D2EHPA, CYANEX® 272 and CYANEX® 302 | en_US |
| dc.type | Text | en_US |
| dc.contributor.department | New Materials, MERC | en_US |
| dc.contributor.department | MMPE, Amirkabir University of Technology | en_US |
| dc.contributor.department | NM, MERC | en_US |
| dc.contributor.department | Materials Science and Engineering, Sharif University of Technology | en_US |
| dc.citation.volume | 24 | |
| dc.citation.issue | 2 | |
| dc.citation.spage | 181 | |
| dc.citation.epage | 190 | |
| nlai.contributor.orcid | 0000-0003-2631-5863 | |