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dc.contributor.authorSenol, A
dc.date.accessioned2021-03-02T23:12:36Z
dc.date.available2021-03-02T23:12:36Z
dc.date.issued2002
dc.identifier.citationSenol A., "Extraction equilibria of valeric acid using (Alamine 336/diluent) and conventional solvent systems. Modeling considerations", CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, cilt.41, sa.8, ss.681-692, 2002
dc.identifier.issn0255-2701
dc.identifier.othervv_1032021
dc.identifier.otherav_11143779-757a-429e-ba9d-d9a5f93c1103
dc.identifier.urihttp://hdl.handle.net/20.500.12627/16978
dc.identifier.urihttps://doi.org/10.1016/s0255-2701(01)00188-x
dc.description.abstractDistribution of valeric acid between water and Alamine 336, a mixture of tertiary aliphatic amines dissolved in various (proton-donating and -accepting, polar and nonpolar) diluents, as well as a comparison with the extraction equilibria of pure diluent alone, have been studied at 298 K. The influence of the acid structure over distribution has been interpreted through comparing the extractabilities of four acids containing different functional groups, i.e. valeric, formic, levulinic and nicotinic acids. The results were correlated using a modified linear solvation energy relation (METLER) and various versions of the mass action law, i.e. a chemodel approach and a modified Langmuir equilibrium model comprising the formation of one or two acids per multiple amines aggregated structures. The reliability of the proposed extraction models has been analyzed statistically on the basis of the overall loading factor of amine, Z(t), using a log-ratio objective function. (C) 2002 Elsevier Science B.V. All rights reserved.
dc.language.isoeng
dc.subjectBiyoyakıt Teknolojisi
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectMühendislik ve Teknoloji
dc.subjectZiraat
dc.subjectTarımda Enerji
dc.subjectTarım Makineleri
dc.subjectTarımsal Bilimler
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMühendislik
dc.subjectENERJİ VE YAKITLAR
dc.titleExtraction equilibria of valeric acid using (Alamine 336/diluent) and conventional solvent systems. Modeling considerations
dc.typeMakale
dc.relation.journalCHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION
dc.contributor.department, ,
dc.identifier.volume41
dc.identifier.issue8
dc.identifier.startpage681
dc.identifier.endpage692
dc.contributor.firstauthorID165828


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