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Isothermal Vapour-Liquid Equilibria in the Binary and Ternary Systems Composed of 2,2,4-Trimethylpentane, 2-Methyl-1-Propanol, and 4-Methyl-2-Pentanone
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SYSNO ASEP 0361004 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 2,2,4-Trimethylpentane, 2-Methyl-1-Propanol, and 4-Methyl-2-Pentanone Author(s) Bernatová, Svatoslava (UCHP-M)
Pavlíček, Jan (UCHP-M) RID, SAI
Wichterle, Ivan (UCHP-M) RID, ORCID, SAISource Title Fluid Phase Equilibria. - : Elsevier - ISSN 0378-3812
Roč. 307, č. 1 (2011), s. 66-71Number of pages 6 s. Language eng - English Country NL - Netherlands Keywords vapor-liquid equilibrium ; experimental data ; prediction 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 000294194700011 DOI 10.1016/j.fluid.2011.05.011 Annotation Vapour–liquid equilibrium data in the three binary 2,2,4-trimethylpentane + 2-methyl-1-propanol, 2-methyl-1-propanol + 2,2-dimethyl-1-propanol, 2,2,4-trimethylpentane + 4-methyl-2-pentanone systems, and in the ternary 2,2,4-trimethylpentane + 2-methyl-1-propanol + 4-methyl-2-pentanone system are reported. The data were measured isothermally at 333.15, 348.15 and 364.15 K covering the pressure range 12–100 kPa. The binary vapour–liquid equilibrium data were correlated using the Wilson and NRTL equations by means of a robust algorithm for processing all isotherms together; 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 2012
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