Loading…

Solvent Extraction of Nickel and Zinc from Nitric Acid Solution Using D2EHPA: Experimental and Modeling

The present communication investigates the reaction mechanism of extraction of Zn(II) and Ni(II) and thermodynamic modeling using di-(2-ethylhexyl) phosphoric acid (D2EHPA) as an organic extractant that is diluted in kerosene at T  = 25 °C and the organic: aqueous phase ratio of 1:1 and pH range 2–6...

Full description

Saved in:
Bibliographic Details
Published in:Journal of solution chemistry 2022, Vol.51 (4), p.424-447
Main Authors: Mohammadzadeh, Masumeh, Bagheri, Hamidreza, Ghader, Sattar
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by cdi_FETCH-LOGICAL-c319t-d26c20c9b4b275f5542b62c726b78a8a4b92ef88f8da974555887ebd425bbb9e3
cites cdi_FETCH-LOGICAL-c319t-d26c20c9b4b275f5542b62c726b78a8a4b92ef88f8da974555887ebd425bbb9e3
container_end_page 447
container_issue 4
container_start_page 424
container_title Journal of solution chemistry
container_volume 51
creator Mohammadzadeh, Masumeh
Bagheri, Hamidreza
Ghader, Sattar
description The present communication investigates the reaction mechanism of extraction of Zn(II) and Ni(II) and thermodynamic modeling using di-(2-ethylhexyl) phosphoric acid (D2EHPA) as an organic extractant that is diluted in kerosene at T  = 25 °C and the organic: aqueous phase ratio of 1:1 and pH range 2–6. The effect of two important parameters i.e. concentration of extractant and pH on the extraction of metals were investigated. The experimental tests allowed us to define the best process conditions, among various investigated conditions, to extract Ni(II) and Zn(II) from filter cake. The optimized extraction values of Ni(II) and Zn(II) were 95.5 and 95.1%, respectively and these were obtained within one stage by 25% (v/v) concentration of D2EHPA, 60 min of contact time and rotation speed of 600 rpm. Moreover, the extraction reaction stoichiometry of Ni(II) and Zn(II) was determined using the slope analysis. Also, the activity coefficient of all ions in the aqueous phase and all of the organic components in the organic phase were predicted based on Electrolyte- universal quasichemical-NRF and universal quasichemical-NRF model. The obtained results indicated well agreement with the experimental data.
doi_str_mv 10.1007/s10953-022-01151-5
format article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_journals_2647680353</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>2647680353</sourcerecordid><originalsourceid>FETCH-LOGICAL-c319t-d26c20c9b4b275f5542b62c726b78a8a4b92ef88f8da974555887ebd425bbb9e3</originalsourceid><addsrcrecordid>eNp9kE9PwyAYh4nRxDn9Ap5IPKPwthTwtszpTOafRHfxQoDSpbNrJ3RGv71oTbx5Ii_v8_wgP4ROGT1nlIqLyKjiGaEAhDLGGeF7aMS4ACIViH00omlPlJBwiI5iXNM0S5WP0Oqpa9592-PZRx-M6-uuxV2F72v36hts2hK_1K3DVeg26bIPtcMTV5c4absfeBnrdoWvYDZ_nFymlK0P9SYFmsG-60rfJOIYHVSmif7k9xyj5fXseToni4eb2-lkQVzGVE9KKBxQp2xuQfCK8xxsAU5AYYU00uRWga-krGRplMg551IKb8scuLVW-WyMzobcbejedj72et3tQpue1FDkopA041miYKBc6GIMvtLb9GsTPjWj-rtQPRSqU6H6p1DNk5QNUkxwu_LhL_of6wvY7Xfy</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2647680353</pqid></control><display><type>article</type><title>Solvent Extraction of Nickel and Zinc from Nitric Acid Solution Using D2EHPA: Experimental and Modeling</title><source>Springer Nature</source><creator>Mohammadzadeh, Masumeh ; Bagheri, Hamidreza ; Ghader, Sattar</creator><creatorcontrib>Mohammadzadeh, Masumeh ; Bagheri, Hamidreza ; Ghader, Sattar</creatorcontrib><description>The present communication investigates the reaction mechanism of extraction of Zn(II) and Ni(II) and thermodynamic modeling using di-(2-ethylhexyl) phosphoric acid (D2EHPA) as an organic extractant that is diluted in kerosene at T  = 25 °C and the organic: aqueous phase ratio of 1:1 and pH range 2–6. The effect of two important parameters i.e. concentration of extractant and pH on the extraction of metals were investigated. The experimental tests allowed us to define the best process conditions, among various investigated conditions, to extract Ni(II) and Zn(II) from filter cake. The optimized extraction values of Ni(II) and Zn(II) were 95.5 and 95.1%, respectively and these were obtained within one stage by 25% (v/v) concentration of D2EHPA, 60 min of contact time and rotation speed of 600 rpm. Moreover, the extraction reaction stoichiometry of Ni(II) and Zn(II) was determined using the slope analysis. Also, the activity coefficient of all ions in the aqueous phase and all of the organic components in the organic phase were predicted based on Electrolyte- universal quasichemical-NRF and universal quasichemical-NRF model. The obtained results indicated well agreement with the experimental data.</description><identifier>ISSN: 0095-9782</identifier><identifier>EISSN: 1572-8927</identifier><identifier>DOI: 10.1007/s10953-022-01151-5</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>Activity coefficients ; Chemistry ; Chemistry and Materials Science ; Condensed Matter Physics ; Filter cake ; Geochemistry ; Industrial Chemistry/Chemical Engineering ; Inorganic Chemistry ; Modelling ; Nitric acid ; Oceanography ; Phase ratio ; Phosphoric acid ; Physical Chemistry ; Reaction mechanisms ; Solvent extraction ; Stoichiometry ; Thermodynamic models ; Zinc</subject><ispartof>Journal of solution chemistry, 2022, Vol.51 (4), p.424-447</ispartof><rights>The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022</rights><rights>The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c319t-d26c20c9b4b275f5542b62c726b78a8a4b92ef88f8da974555887ebd425bbb9e3</citedby><cites>FETCH-LOGICAL-c319t-d26c20c9b4b275f5542b62c726b78a8a4b92ef88f8da974555887ebd425bbb9e3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,777,781,27905,27906</link.rule.ids></links><search><creatorcontrib>Mohammadzadeh, Masumeh</creatorcontrib><creatorcontrib>Bagheri, Hamidreza</creatorcontrib><creatorcontrib>Ghader, Sattar</creatorcontrib><title>Solvent Extraction of Nickel and Zinc from Nitric Acid Solution Using D2EHPA: Experimental and Modeling</title><title>Journal of solution chemistry</title><addtitle>J Solution Chem</addtitle><description>The present communication investigates the reaction mechanism of extraction of Zn(II) and Ni(II) and thermodynamic modeling using di-(2-ethylhexyl) phosphoric acid (D2EHPA) as an organic extractant that is diluted in kerosene at T  = 25 °C and the organic: aqueous phase ratio of 1:1 and pH range 2–6. The effect of two important parameters i.e. concentration of extractant and pH on the extraction of metals were investigated. The experimental tests allowed us to define the best process conditions, among various investigated conditions, to extract Ni(II) and Zn(II) from filter cake. The optimized extraction values of Ni(II) and Zn(II) were 95.5 and 95.1%, respectively and these were obtained within one stage by 25% (v/v) concentration of D2EHPA, 60 min of contact time and rotation speed of 600 rpm. Moreover, the extraction reaction stoichiometry of Ni(II) and Zn(II) was determined using the slope analysis. Also, the activity coefficient of all ions in the aqueous phase and all of the organic components in the organic phase were predicted based on Electrolyte- universal quasichemical-NRF and universal quasichemical-NRF model. The obtained results indicated well agreement with the experimental data.</description><subject>Activity coefficients</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Condensed Matter Physics</subject><subject>Filter cake</subject><subject>Geochemistry</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Inorganic Chemistry</subject><subject>Modelling</subject><subject>Nitric acid</subject><subject>Oceanography</subject><subject>Phase ratio</subject><subject>Phosphoric acid</subject><subject>Physical Chemistry</subject><subject>Reaction mechanisms</subject><subject>Solvent extraction</subject><subject>Stoichiometry</subject><subject>Thermodynamic models</subject><subject>Zinc</subject><issn>0095-9782</issn><issn>1572-8927</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2022</creationdate><recordtype>article</recordtype><recordid>eNp9kE9PwyAYh4nRxDn9Ap5IPKPwthTwtszpTOafRHfxQoDSpbNrJ3RGv71oTbx5Ii_v8_wgP4ROGT1nlIqLyKjiGaEAhDLGGeF7aMS4ACIViH00omlPlJBwiI5iXNM0S5WP0Oqpa9592-PZRx-M6-uuxV2F72v36hts2hK_1K3DVeg26bIPtcMTV5c4absfeBnrdoWvYDZ_nFymlK0P9SYFmsG-60rfJOIYHVSmif7k9xyj5fXseToni4eb2-lkQVzGVE9KKBxQp2xuQfCK8xxsAU5AYYU00uRWga-krGRplMg551IKb8scuLVW-WyMzobcbejedj72et3tQpue1FDkopA041miYKBc6GIMvtLb9GsTPjWj-rtQPRSqU6H6p1DNk5QNUkxwu_LhL_of6wvY7Xfy</recordid><startdate>2022</startdate><enddate>2022</enddate><creator>Mohammadzadeh, Masumeh</creator><creator>Bagheri, Hamidreza</creator><creator>Ghader, Sattar</creator><general>Springer US</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>2022</creationdate><title>Solvent Extraction of Nickel and Zinc from Nitric Acid Solution Using D2EHPA: Experimental and Modeling</title><author>Mohammadzadeh, Masumeh ; Bagheri, Hamidreza ; Ghader, Sattar</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c319t-d26c20c9b4b275f5542b62c726b78a8a4b92ef88f8da974555887ebd425bbb9e3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2022</creationdate><topic>Activity coefficients</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Condensed Matter Physics</topic><topic>Filter cake</topic><topic>Geochemistry</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Inorganic Chemistry</topic><topic>Modelling</topic><topic>Nitric acid</topic><topic>Oceanography</topic><topic>Phase ratio</topic><topic>Phosphoric acid</topic><topic>Physical Chemistry</topic><topic>Reaction mechanisms</topic><topic>Solvent extraction</topic><topic>Stoichiometry</topic><topic>Thermodynamic models</topic><topic>Zinc</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mohammadzadeh, Masumeh</creatorcontrib><creatorcontrib>Bagheri, Hamidreza</creatorcontrib><creatorcontrib>Ghader, Sattar</creatorcontrib><collection>CrossRef</collection><jtitle>Journal of solution chemistry</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mohammadzadeh, Masumeh</au><au>Bagheri, Hamidreza</au><au>Ghader, Sattar</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Solvent Extraction of Nickel and Zinc from Nitric Acid Solution Using D2EHPA: Experimental and Modeling</atitle><jtitle>Journal of solution chemistry</jtitle><stitle>J Solution Chem</stitle><date>2022</date><risdate>2022</risdate><volume>51</volume><issue>4</issue><spage>424</spage><epage>447</epage><pages>424-447</pages><issn>0095-9782</issn><eissn>1572-8927</eissn><abstract>The present communication investigates the reaction mechanism of extraction of Zn(II) and Ni(II) and thermodynamic modeling using di-(2-ethylhexyl) phosphoric acid (D2EHPA) as an organic extractant that is diluted in kerosene at T  = 25 °C and the organic: aqueous phase ratio of 1:1 and pH range 2–6. The effect of two important parameters i.e. concentration of extractant and pH on the extraction of metals were investigated. The experimental tests allowed us to define the best process conditions, among various investigated conditions, to extract Ni(II) and Zn(II) from filter cake. The optimized extraction values of Ni(II) and Zn(II) were 95.5 and 95.1%, respectively and these were obtained within one stage by 25% (v/v) concentration of D2EHPA, 60 min of contact time and rotation speed of 600 rpm. Moreover, the extraction reaction stoichiometry of Ni(II) and Zn(II) was determined using the slope analysis. Also, the activity coefficient of all ions in the aqueous phase and all of the organic components in the organic phase were predicted based on Electrolyte- universal quasichemical-NRF and universal quasichemical-NRF model. The obtained results indicated well agreement with the experimental data.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s10953-022-01151-5</doi><tpages>24</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0095-9782
ispartof Journal of solution chemistry, 2022, Vol.51 (4), p.424-447
issn 0095-9782
1572-8927
language eng
recordid cdi_proquest_journals_2647680353
source Springer Nature
subjects Activity coefficients
Chemistry
Chemistry and Materials Science
Condensed Matter Physics
Filter cake
Geochemistry
Industrial Chemistry/Chemical Engineering
Inorganic Chemistry
Modelling
Nitric acid
Oceanography
Phase ratio
Phosphoric acid
Physical Chemistry
Reaction mechanisms
Solvent extraction
Stoichiometry
Thermodynamic models
Zinc
title Solvent Extraction of Nickel and Zinc from Nitric Acid Solution Using D2EHPA: Experimental and Modeling
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-17T20%3A48%3A28IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Solvent%20Extraction%20of%20Nickel%20and%20Zinc%20from%20Nitric%20Acid%20Solution%20Using%20D2EHPA:%20Experimental%20and%20Modeling&rft.jtitle=Journal%20of%20solution%20chemistry&rft.au=Mohammadzadeh,%20Masumeh&rft.date=2022&rft.volume=51&rft.issue=4&rft.spage=424&rft.epage=447&rft.pages=424-447&rft.issn=0095-9782&rft.eissn=1572-8927&rft_id=info:doi/10.1007/s10953-022-01151-5&rft_dat=%3Cproquest_cross%3E2647680353%3C/proquest_cross%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c319t-d26c20c9b4b275f5542b62c726b78a8a4b92ef88f8da974555887ebd425bbb9e3%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=2647680353&rft_id=info:pmid/&rfr_iscdi=true