| dc.contributor.author | Senol, A | |
| dc.date.accessioned | 2021-03-06T21:18:45Z | |
| dc.date.available | 2021-03-06T21:18:45Z | |
| dc.date.issued | 2005 | |
| dc.identifier.citation | Senol A., "Phase equilibria for ternary liquid systems of (water plus levulinic acid plus cyclic solvent) at T=298.2 K: Thermodynamic modeling", JOURNAL OF CHEMICAL THERMODYNAMICS, cilt.37, ss.1104-1110, 2005 | |
| dc.identifier.issn | 0021-9614 | |
| dc.identifier.other | av_fe1b7774-a3c8-4141-a965-8018e58af66a | |
| dc.identifier.other | vv_1032021 | |
| dc.identifier.uri | http://hdl.handle.net/20.500.12627/166202 | |
| dc.identifier.uri | https://doi.org/10.1016/j.jct.2005.01.014 | |
| dc.description.abstract | (Liquid + liquid) equilibrium (LLE) data of the solubility curves and tie-line end compositions are presented for mixtures of {water (1) + levulinic acid (2) + methylcyclohexanol, or cyclohexanone, or cyclohexyl acetate (3)} at T = 298.2 K and P = (101.3 +/- 0.7) kPa. Among the studied C6 ring-containing cyclic solvents, methylcyclohexanol and cyclohexyl acetate give the largest distribution ratio and separation factors for extraction of levulinic acid. A solvation energy relation (SERLAS) has been used to estimate the (liquid + liquid) equilibria of associated systems containing components capable of a physical interaction through hydrogen bonding. The tie-lines were also predicted using the UNIFAC-original model. The reliability of both models has been analyzed against the LLE data with respect to the distribution ratio and separation factor. SERLAS matches LLE data quite accurately, yielding a mean error of 3.6% for all the systems considered. (c) 2005 Elsevier Ltd. All rights reserved. | |
| dc.language.iso | eng | |
| dc.subject | Mühendislik, Bilişim ve Teknoloji (ENG) | |
| dc.subject | TERMODİNAMİK | |
| dc.subject | Mühendislik | |
| dc.subject | KİMYA, FİZİKSEL | |
| dc.subject | Kimya | |
| dc.subject | Temel Bilimler (SCI) | |
| dc.subject | Fizikokimya | |
| dc.subject | Temel Bilimler | |
| dc.subject | Mühendislik ve Teknoloji | |
| dc.title | Phase equilibria for ternary liquid systems of (water plus levulinic acid plus cyclic solvent) at T=298.2 K: Thermodynamic modeling | |
| dc.type | Makale | |
| dc.relation.journal | JOURNAL OF CHEMICAL THERMODYNAMICS | |
| dc.contributor.department | , , | |
| dc.identifier.volume | 37 | |
| dc.identifier.issue | 10 | |
| dc.identifier.startpage | 1104 | |
| dc.identifier.endpage | 1110 | |
| dc.contributor.firstauthorID | 176295 | |