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dc.contributor.authorUslu, Hasan
dc.contributor.authorKirbaslar, S. Ismail
dc.date.accessioned2021-03-06T09:44:04Z
dc.date.available2021-03-06T09:44:04Z
dc.date.issued2008
dc.identifier.citationUslu H., Kirbaslar S. I. , "Equilibrium studies of extraction of levulinic acid by (trioctylamine (TOA) plus ester) solvents", JOURNAL OF CHEMICAL AND ENGINEERING DATA, cilt.53, ss.1557-1563, 2008
dc.identifier.issn0021-9568
dc.identifier.otherav_e6e50360-da78-4960-aaa0-169cda7f18de
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/151877
dc.identifier.urihttps://doi.org/10.1021/je800099a
dc.description.abstractReactive extraction of levulinic acid has been done at 298.15 K. All experiments are reported on the extraction of levulinic acid by trioctylamine JOA) dissolved in I I different ester solvents (ethyl propionate, dimethyl phthalate, hexyl acetate, cyclohexyl acetate, dimethyl adipate, propyl acetate,, dimethyl glutarate, dimethyl fumarate, diethyl sebacate, and diethyl carbonate), as well as single solvents. Experimental results of batch extraction experiments are calculated and reported as distribution coefficients (K-D= (c) over bar (HA)/C-HA,C-total), loading factors (TT), stoichiometric loading factor (T-s), separation factor (S-f), and extraction efficiency (E). The diethyl carbonate was found to be the most effective solvent with a maximum distribution value of 5.75. Maximum values of possible equilibrium complexation constants for (acid + amine) (1:1) K, and (2:1) K-21 were determined as 3.32 and 32.59 for diethyl carbonate, respectively.
dc.language.isoeng
dc.subjectBiyokimya
dc.subjectAlkoloidler
dc.subjectTemel Bilimler
dc.subjectMühendislik ve Teknoloji
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectTemel Bilimler (SCI)
dc.subjectKimya
dc.subjectKİMYA, MULTİDİSİPLİNER
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMühendislik
dc.subjectTERMODİNAMİK
dc.titleEquilibrium studies of extraction of levulinic acid by (trioctylamine (TOA) plus ester) solvents
dc.typeMakale
dc.relation.journalJOURNAL OF CHEMICAL AND ENGINEERING DATA
dc.contributor.departmentBeykent Üniversitesi , ,
dc.identifier.volume53
dc.identifier.issue7
dc.identifier.startpage1557
dc.identifier.endpage1563
dc.contributor.firstauthorID48765


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