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dc.contributor.authorSenol, A
dc.date.accessioned2021-03-05T18:01:00Z
dc.date.available2021-03-05T18:01:00Z
dc.date.issued2003
dc.identifier.citationSenol A., "Liquid-liquid extraction of isovaleric acid using Alamine 308/diluent and conventional solvent systems: Effect of diluent and acid structure", SOLVENT EXTRACTION AND ION EXCHANGE, cilt.21, ss.853-879, 2003
dc.identifier.issn0736-6299
dc.identifier.otherav_c8584717-16bf-4c67-bc15-c177e425d22e
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/132768
dc.identifier.urihttps://doi.org/10.1081/sei-120025929
dc.description.abstractDistribution of isovaleric (3-methyl butanoic) acid between water and Alamine 308 (triisooctylamine) dissolved in C-5 and C-6-ring included diluents of proton-donating and -accepting (cyclopentanol, cyclohexanone), polar (chlorobenzene) and inert (toluene) types, as well as a comparison with the extraction equilibria of pure diluent alone (chloroform) have been studied at 298 K. Among the tested C-6 ring-containing and aliphatic diluents, cyclic alcohol/amine system yields the highest synergistic extraction efficiency. The strength of the complex solvation was found to be reasonably large for halogenated aromatics favoring mainly the formation of acid(1)-amine(2) structure. The influence of the acid structure over distribution has been interpreted through comparing the extractabilities of seven acids containing different functional groups, i.e., isovaleric, formic, levulinic, acetic, propanoic, pyruvic and nicotinic acids. The results were correlated using a modified linear solvation energy relation (METLER) and versions of the mass action law, i.e., a chemodel approach and a modified Langmuir equilibrium model comprising the formation of one or two acid-multiple amines complex formation.
dc.language.isoeng
dc.subjectTemel Bilimler (SCI)
dc.subjectAlkoloidler
dc.subjectKİMYA, MULTİDİSİPLİNER
dc.subjectKimya
dc.subjectBiyokimya
dc.subjectTemel Bilimler
dc.titleLiquid-liquid extraction of isovaleric acid using Alamine 308/diluent and conventional solvent systems: Effect of diluent and acid structure
dc.typeMakale
dc.relation.journalSOLVENT EXTRACTION AND ION EXCHANGE
dc.contributor.department, ,
dc.identifier.volume21
dc.identifier.issue6
dc.identifier.startpage853
dc.identifier.endpage879
dc.contributor.firstauthorID166948


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