| dc.contributor.author | Senol, A | |
| dc.date.accessioned | 2021-03-05T19:34:22Z | |
| dc.date.available | 2021-03-05T19:34:22Z | |
| dc.date.issued | 2005 | |
| dc.identifier.citation | Senol A., "Phase equilibria for ternary liquid systems of (water plus carboxylic acid+1-heptanol) at 293.15K: Modelling considerations", CANADIAN JOURNAL OF CHEMICAL ENGINEERING, cilt.83, ss.962-969, 2005 | |
| dc.identifier.issn | 0008-4034 | |
| dc.identifier.other | vv_1032021 | |
| dc.identifier.other | av_cfe3e5b1-5e36-4a52-8488-5a24f2a5073b | |
| dc.identifier.uri | http://hdl.handle.net/20.500.12627/137448 | |
| dc.description.abstract | Liquid-liquid equilibrium data of the solubility curves and tie-line end compositions are presented for mixtures of [water (1) + formic acid, or acetic acid, or propanoic acid (2) + 1-heptanol (3)] at T = 293.15 K and P = (1101.3 +/- 0.7) kPa. The properties and liquid-liquid equilibria (LLE) of associated ternary systems have been correlated using a solvatochromic approach SERLAS. The tie-lines were also predicted using the UNIFAC-original model. The proposed model appears to be an improvement in data fit for the ternary systems yielding a mean error of 3.8% for all the systems considered. | |
| dc.language.iso | eng | |
| dc.subject | Mühendislik | |
| dc.subject | Mühendislik, Bilişim ve Teknoloji (ENG) | |
| dc.subject | Kimya Mühendisliği ve Teknolojisi | |
| dc.subject | Mühendislik ve Teknoloji | |
| dc.subject | MÜHENDİSLİK, KİMYASAL | |
| dc.title | Phase equilibria for ternary liquid systems of (water plus carboxylic acid+1-heptanol) at 293.15K: Modelling considerations | |
| dc.type | Makale | |
| dc.relation.journal | CANADIAN JOURNAL OF CHEMICAL ENGINEERING | |
| dc.contributor.department | , , | |
| dc.identifier.volume | 83 | |
| dc.identifier.issue | 6 | |
| dc.identifier.startpage | 962 | |
| dc.identifier.endpage | 969 | |
| dc.contributor.firstauthorID | 176716 | |
