dc.contributor.author | Dramur, U | |
dc.contributor.author | Cehreli, S | |
dc.contributor.author | Ozmen, D | |
dc.date.accessioned | 2021-03-04T13:52:47Z | |
dc.date.available | 2021-03-04T13:52:47Z | |
dc.date.issued | 2006 | |
dc.identifier.citation | Cehreli S., Ozmen D., Dramur U., "(Liquid plus liquid) equilibria of (water plus 1-propanol plus solvent) at T=298.2 K", FLUID PHASE EQUILIBRIA, cilt.239, sa.2, ss.156-160, 2006 | |
dc.identifier.issn | 0378-3812 | |
dc.identifier.other | vv_1032021 | |
dc.identifier.other | av_7eade819-add3-4045-8cdd-9a93db09b0f6 | |
dc.identifier.uri | http://hdl.handle.net/20.500.12627/86486 | |
dc.identifier.uri | https://doi.org/10.1016/j.fluid.2005.11.024 | |
dc.description.abstract | (Liquid + liquid) equilibrium (LLE) data for (water-1-propanol-solvent) were measured at T = 298.2 K and atmospheric pressure. Thesolvents were methyl acetate, ethyl acetate and n-propyl acetate. The UNIQUAC and UNIFAC models were used to correlate the experimental data. A comparison of the extracting capabilities of the solvents was made with respect to distribution coefficients, separation factors. (c) 2005 Elsevier B.V. All rights reserved. | |
dc.language.iso | eng | |
dc.subject | Fizikokimya | |
dc.subject | Mühendislik ve Teknoloji | |
dc.subject | Temel Bilimler | |
dc.subject | TERMODİNAMİK | |
dc.subject | Mühendislik | |
dc.subject | Mühendislik, Bilişim ve Teknoloji (ENG) | |
dc.subject | KİMYA, FİZİKSEL | |
dc.subject | Kimya | |
dc.subject | Temel Bilimler (SCI) | |
dc.subject | MÜHENDİSLİK, KİMYASAL | |
dc.subject | Kimya Mühendisliği ve Teknolojisi | |
dc.title | (Liquid plus liquid) equilibria of (water plus 1-propanol plus solvent) at T=298.2 K | |
dc.type | Makale | |
dc.relation.journal | FLUID PHASE EQUILIBRIA | |
dc.contributor.department | , , | |
dc.identifier.volume | 239 | |
dc.identifier.issue | 2 | |
dc.identifier.startpage | 156 | |
dc.identifier.endpage | 160 | |
dc.contributor.firstauthorID | 177082 | |