Basit öğe kaydını göster

dc.contributor.authorSenol, A
dc.date.accessioned2021-03-05T18:56:44Z
dc.date.available2021-03-05T18:56:44Z
dc.date.issued1999
dc.identifier.citationSenol A., "Extraction equilibria of formic, levulinic and acetic acids using (Alamine 336/diluent) and conventional solvent systems: Modeling considerations", JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, cilt.32, ss.717-731, 1999
dc.identifier.issn0021-9592
dc.identifier.otherav_ccd6e70d-d8f4-4bf6-a5b4-3ccc25ecb264
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/135600
dc.identifier.urihttps://doi.org/10.1252/jcej.32.717
dc.description.abstractDistribution of formic, levulinic and acetic acids 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 are studied at 25 degrees C. The influence of the acid structure over distribution is evaluated through comparing the extractabilities of five acids containing different functional groups, namely, formic, levulinic, acetic, valeric and nicotinic acids. The results were correlated using a modified linear solvation energy relation (LSER) and various versions of the mass action law namely, a chemical modeling approach and a modified version of the Langmuir equilibrium model comprising one or two acid-amine complex formations. Details underlying some aspects of selection of an appropriate algorithm for fitting the data are discussed. Finally, the reliability of the proposed extraction models is analyzed statistically on the basis of the overall loading factor of amine, Z(t), using a log-ratio objective function.
dc.language.isoeng
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMühendislik ve Teknoloji
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectMühendislik
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.titleExtraction equilibria of formic, levulinic and acetic acids using (Alamine 336/diluent) and conventional solvent systems: Modeling considerations
dc.typeMakale
dc.relation.journalJOURNAL OF CHEMICAL ENGINEERING OF JAPAN
dc.contributor.department, ,
dc.identifier.volume32
dc.identifier.issue6
dc.identifier.startpage717
dc.identifier.endpage731
dc.contributor.firstauthorID124318


Bu öğenin dosyaları:

DosyalarBoyutBiçimGöster

Bu öğe ile ilişkili dosya yok.

Bu öğe aşağıdaki koleksiyon(lar)da görünmektedir.

Basit öğe kaydını göster