EXTRACTION OF URANYL NITRATE WITH N,N-DIBUTYL-2--ETHYLHEXYL AMIDE
The extraction of nitric acid and uranyl nitrate with N,N-dibutyl-2-ethylhexyl amide (DBEHA) has been studied. The solvates formed in the organic phase are HN03-DBEHA and U02(NO3) 2.2DBEHA with the corresponding complex formation constants 0.05 and 20, respectively. The increase of uranyl nitrate di...
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Veröffentlicht in: | Solvent extraction and ion exchange 1986-01, Vol.4 (3), p.435-448 |
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creator | Kopecni, Miroslav M. Petkovid, Djordje M. |
description | The extraction of nitric acid and uranyl nitrate with N,N-dibutyl-2-ethylhexyl amide (DBEHA) has been studied. The solvates formed in the organic phase are HN03-DBEHA and U02(NO3) 2.2DBEHA with the corresponding complex formation constants 0.05 and 20, respectively. The increase of uranyl nitrate distribution with the increase of nitric acid concentration in the aqueous phase, has been interpreted as the influence of nitrate ions on the extraction equilibrium. |
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The solvates formed in the organic phase are HN03-DBEHA and U02(NO3) 2.2DBEHA with the corresponding complex formation constants 0.05 and 20, respectively. The increase of uranyl nitrate distribution with the increase of nitric acid concentration in the aqueous phase, has been interpreted as the influence of nitrate ions on the extraction equilibrium.</description><identifier>ISSN: 0736-6299</identifier><identifier>EISSN: 1532-2262</identifier><identifier>DOI: 10.1080/07366298608917876</identifier><language>eng</language><publisher>Taylor & Francis Group</publisher><ispartof>Solvent extraction and ion exchange, 1986-01, Vol.4 (3), p.435-448</ispartof><rights>Copyright Taylor & Francis Group, LLC 1986</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c296t-c06d0dc087eefaf6bf2abbd46fdb600e2ac55218a8450fee8d1fccaeba54e73d3</citedby><cites>FETCH-LOGICAL-c296t-c06d0dc087eefaf6bf2abbd46fdb600e2ac55218a8450fee8d1fccaeba54e73d3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.tandfonline.com/doi/pdf/10.1080/07366298608917876$$EPDF$$P50$$Ginformaworld$$H</linktopdf><linktohtml>$$Uhttps://www.tandfonline.com/doi/full/10.1080/07366298608917876$$EHTML$$P50$$Ginformaworld$$H</linktohtml><link.rule.ids>314,780,784,27922,27923,59645,60434</link.rule.ids></links><search><creatorcontrib>Kopecni, Miroslav M.</creatorcontrib><creatorcontrib>Petkovid, Djordje M.</creatorcontrib><title>EXTRACTION OF URANYL NITRATE WITH N,N-DIBUTYL-2--ETHYLHEXYL AMIDE</title><title>Solvent extraction and ion exchange</title><description>The extraction of nitric acid and uranyl nitrate with N,N-dibutyl-2-ethylhexyl amide (DBEHA) has been studied. 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The increase of uranyl nitrate distribution with the increase of nitric acid concentration in the aqueous phase, has been interpreted as the influence of nitrate ions on the extraction equilibrium.</description><issn>0736-6299</issn><issn>1532-2262</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1986</creationdate><recordtype>article</recordtype><recordid>eNp1kM1Kw0AcxBdRsFYfwFsewNX_bpLNBrzENjWBmEDZYHMKm_2ASNvIplD69qbUm3gamJnfHAahRwLPBDi8QOQzRmPOgMck4hG7QjMS-hRTyug1mp1zPBXiW3Q3jl8AJOScz1CSbsQ6WYi8Kr1q5dXrpGwKr8wnU6TeZy4yr3wq8TJ_q0VTYIpxKrKmyNLNVEs-8mV6j26s3I7m4VfnqF6lYpHhonrPF0mBFY3ZAStgGrQCHhljpWWdpbLrdMCs7hiAoVKFISVc8iAEawzXxColTSfDwES-9ueIXHaVG8bRGdt-u34n3akl0J4_aP98MDGvF6bf28Ht5HFwW90e5Gk7OOvkXvVj6_-P_wBUR10Z</recordid><startdate>19860101</startdate><enddate>19860101</enddate><creator>Kopecni, Miroslav M.</creator><creator>Petkovid, Djordje M.</creator><general>Taylor & Francis Group</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>19860101</creationdate><title>EXTRACTION OF URANYL NITRATE WITH N,N-DIBUTYL-2--ETHYLHEXYL AMIDE</title><author>Kopecni, Miroslav M. ; Petkovid, Djordje M.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c296t-c06d0dc087eefaf6bf2abbd46fdb600e2ac55218a8450fee8d1fccaeba54e73d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1986</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kopecni, Miroslav M.</creatorcontrib><creatorcontrib>Petkovid, Djordje M.</creatorcontrib><collection>CrossRef</collection><jtitle>Solvent extraction and ion exchange</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kopecni, Miroslav M.</au><au>Petkovid, Djordje M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>EXTRACTION OF URANYL NITRATE WITH N,N-DIBUTYL-2--ETHYLHEXYL AMIDE</atitle><jtitle>Solvent extraction and ion exchange</jtitle><date>1986-01-01</date><risdate>1986</risdate><volume>4</volume><issue>3</issue><spage>435</spage><epage>448</epage><pages>435-448</pages><issn>0736-6299</issn><eissn>1532-2262</eissn><abstract>The extraction of nitric acid and uranyl nitrate with N,N-dibutyl-2-ethylhexyl amide (DBEHA) has been studied. The solvates formed in the organic phase are HN03-DBEHA and U02(NO3) 2.2DBEHA with the corresponding complex formation constants 0.05 and 20, respectively. The increase of uranyl nitrate distribution with the increase of nitric acid concentration in the aqueous phase, has been interpreted as the influence of nitrate ions on the extraction equilibrium.</abstract><pub>Taylor & Francis Group</pub><doi>10.1080/07366298608917876</doi><tpages>14</tpages></addata></record> |
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title | EXTRACTION OF URANYL NITRATE WITH N,N-DIBUTYL-2--ETHYLHEXYL AMIDE |
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