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Vapour–Liquid Equilibria in the Binary and Ternary Systems Composed of 2,3-Dimethylbutane, Diisopropyl Ether, and 3-Methyl-2-Butanone at 313.15, 323.15 and 313.15 K
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SYSNO ASEP 0390632 Document Type J - Journal Article R&D Document Type Journal Article Subsidiary J Článek ve WOS Title Vapour–Liquid Equilibria in the Binary and Ternary Systems Composed of 2,3-Dimethylbutane, Diisopropyl Ether, and 3-Methyl-2-Butanone at 313.15, 323.15 and 313.15 K Author(s) Pavlíček, Jan (UCHP-M) RID, SAI
Andresová, Adéla (UCHP-M) RID, SAI
Bogdanić, Grozdana (UCHP-M) RID, ORCID, SAI
Wichterle, Ivan (UCHP-M) RID, ORCID, SAISource Title Fluid Phase Equilibria. - : Elsevier - ISSN 0378-3812
Roč. 344, APR 25 (2013), s. 59-64Number of pages 6 s. Language eng - English Country NL - Netherlands Keywords vapour-liquid equilibrium ; prediction ; experimental data Subject RIV CF - Physical ; Theoretical Chemistry Institutional support UCHP-M - RVO:67985858 UT WOS 000317538600009 DOI 10.1016/j.fluid.2013.01.020 Annotation This article reports vapour–liquid equilibrium data in the three binary 2,3-dimethylbutane + diisopropyl ether, 2,3-dimethylbutane + 3-methyl-2-butanone, diisopropyl ether + 3-methyl-2-butanone and in the ternary 2,3-dimethylbutane + diisopropyl ether + 3-methyl-2-butanone systems are reported. The data were measured isothermally at 313.15, 323.15 and 333.15 K covering the pressure range 13–108 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 2014
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