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dc.contributor.authorInci, I
dc.date.accessioned2021-03-04T08:00:44Z
dc.date.available2021-03-04T08:00:44Z
dc.date.issued2002
dc.identifier.citationInci I., "Extraction equilibria of aqueous solution of acetic acid with tri-n-octylamine", JOURNAL OF SCIENTIFIC & INDUSTRIAL RESEARCH, cilt.61, sa.10, ss.817-822, 2002
dc.identifier.issn0022-4456
dc.identifier.othervv_1032021
dc.identifier.otherav_61099031-b18f-4ba6-98d2-b510d5c4c99c
dc.identifier.urihttp://hdl.handle.net/20.500.12627/67688
dc.description.abstractThe extraction of acetic acid from aqueous solutions by tri-n-octylamine dissolved in various diluents in wide range of amine concentration (0.23 - 1.15 mol / L) is studied. Extraction equilibria of acetic acid in the solution of tri-n-octylamine in five various. solvents at 298.15 K is measured., Diluting solvents used in this study are hexane, cyclohexane, toluene, methyl isobutyl ketone (MIBK), and propanol. Using Bizek approach two acids: amine complexes, (Acid), (Amine) and (Acid), (Amine)(2) is are assumed to exist in the organic phase in the case of proton - donating diluents, while the complexes (Acid), (Amine) and (Acid) (2), (Amine)(3) are suggested in the case of non-proton-donating diluents. As a result of batch extraction experiments, distribution coefficients (D), loading factors ( Z), and overall extraction constants (K-11, K-12, K-23) are calculated.
dc.language.isoeng
dc.subjectMühendislik
dc.subjectMühendislik ve Teknoloji
dc.subjectHarita Mühendisliği-Geomatik
dc.subjectMÜHENDİSLİK, MULTİDİSİPLİNER
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.titleExtraction equilibria of aqueous solution of acetic acid with tri-n-octylamine
dc.typeMakale
dc.relation.journalJOURNAL OF SCIENTIFIC & INDUSTRIAL RESEARCH
dc.contributor.departmentİstanbul Üniversitesi , Mühendislik Fakültesi , Kimya Mühendisliği
dc.identifier.volume61
dc.identifier.issue10
dc.identifier.startpage817
dc.identifier.endpage822
dc.contributor.firstauthorID166018


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