| dc.contributor.author | Özmen, Atilla | |
| dc.contributor.author | Çehreli, Süheyla | |
| dc.date.accessioned | 2019-06-28T11:11:37Z | |
| dc.date.available | 2019-06-28T11:11:37Z | |
| dc.date.issued | 2006 | |
| dc.identifier.isbn | 8086059456 | |
| dc.identifier.isbn | 9788086059457 | |
| dc.identifier.uri | https://hdl.handle.net/20.500.12469/1647 | |
| dc.description.abstract | Liquid-liquid equilibrium (LLE) data for water-1-propanol-n-amyl alcohol and water-1-propanol-n-amyl acetate ternaries were measured at T=298.2 K. The UNIFAC model was used to correlate the experimental data. A comparison of the extracting capabilities of the solvents was made with respect to distribution coefficients and separation factors. | en_US] |
| dc.language.iso | eng | en_US |
| dc.rights | info:eu-repo/semantics/closedAccess | en_US |
| dc.subject | 1-propanol | en_US |
| dc.subject | Liquid-liquid equilibria | en_US |
| dc.subject | n-amyl acetate | en_US |
| dc.subject | n-amyl alcohol | en_US |
| dc.subject | UNIFAC method | en_US |
| dc.title | UNIFAC application to water-1-propanol-n-amyl alcohol and n-amyl acetate ternaries | en_US |
| dc.type | conferenceObject | en_US |
| dc.relation.journal | CHISA 2006 - 17th International Congress of Chemical and Process Engineering | en_US |
| dc.department | Fakülteler, Mühendislik ve Doğa Bilimleri Fakültesi, Elektrik-Elektronik Mühendisliği Bölümü | en_US |
| dc.identifier.scopus | 2-s2.0-34748858547 | en_US |
| dc.institutionauthor | Özmen, Atilla | en_US |
| dc.relation.publicationcategory | Konferans Öğesi - Uluslararası - Kurum Öğretim Elemanı | en_US |
