Number of the records: 1
Isothermal Vapour-Liquid Equilibria in the Binary and Ternary Systems Composed of tert-Butyl Methyl Ether, 3,3-Dimethyl-2-butanone and 2,2-Dimethyl-1-propanol
- 1.
SYSNO ASEP 0322757 Document Type J - Journal Article R&D Document Type Journal Article Subsidiary J Článek ve WOS Title Isothermal Vapour-Liquid Equilibria in the Binary and Ternary Systems Composed of tert-Butyl Methyl Ether, 3,3-Dimethyl-2-butanone and 2,2-Dimethyl-1-propanol Title Izotermní rovnováhy kapalina pára v soustavách tvořených tert-butyl methyl etherem, 3,3-dimethyl-2-butanonem a 2,2-dimethyl-1-propanolem Author(s) Bernatová, Svatoslava (UCHP-M)
Pavlíček, Jan (UCHP-M) RID, SAI
Wichterle, Ivan (UCHP-M) RID, ORCID, SAINumber of authors 3 Source Title Fluid Phase Equilibria. - : Elsevier - ISSN 0378-3812
Roč. 278, 1-2 (2009), s. 129-134Number of pages 6 s. Language eng - English Country NL - Netherlands Keywords alcohol ; ether ; ketone Subject RIV CF - Physical ; Theoretical Chemistry R&D Projects GA104/07/0444 GA ČR - Czech Science Foundation (CSF) CEZ AV0Z40720504 - UCHP-M (2005-2011) UT WOS 000265175900018 DOI 10.1016/j.fluid.2009.01.016 Annotation Vapour–liquid equilibrium data in the three binary tert-butyl methyl ether plus 3,3-dimethyl-2-butanone, 3,3-dimethyl-2-butanone plus 2,2-dimethyl-1-propanol, tert-butyl methyl ether plus 2,2-dimethyl-1-propanol systems, and in the ternary tert-butyl methyl ether plus 3,3-dimethyl-2-butanone plus 2,2-dimethyl-1-propanol system are reported. The data were measured isothermally at 320.00, 330.00 and 340.00 K covering the pressure range 12–118 kPa. The binary vapour–liquid equilibrium data were correlated using the Wilson and NRTL equations by means of a new algorithm; resulting parameters were then used for calculation of phase behaviour in the ternary system and for subsequent comparison with experimental data. Workplace Institute of Chemical Process Fundamentals Contact Eva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227 Year of Publishing 2009
Number of the records: 1