2004
DOI: 10.1016/j.fluid.2004.09.024
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A systematic study of methanol+n-alkane vapor–liquid and liquid–liquid equilibria using the CK-SAFT and PC-SAFT equations of state

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Cited by 57 publications
(44 citation statements)
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“…Moreover, increasing k ij /T trend has been reported for two SAFT variants by Yarrison and Chapman 93 for methanol−alkanes.…”
Section: Discussionmentioning
confidence: 69%
“…Moreover, increasing k ij /T trend has been reported for two SAFT variants by Yarrison and Chapman 93 for methanol−alkanes.…”
Section: Discussionmentioning
confidence: 69%
“…Instead, we use a nomenclature, where association schemes are defined by the total number of associating sites, x, the number of proton acceptor sites, y, and the number of proton donor sites, z, written as x(y:z). This definition is identical to the one used by Yarrison and Chapman 17 and by Avlund et al 18 Three glycolethers have been considered in this work: 2-methoxyethanol (C 1 E 1 ), 2-ethoxyethanol (C 2 E 1 ), and 2-butoxyethanol (C 4 E 1 ). The structures of the three glycol ethers are shown in Figure 3.…”
Section: Articlementioning
confidence: 95%
“…Most studies use either the two-site (2B) or the three-site (3B) scheme [2,3,5,7,8,14], but the best phase equilibrium results are obtained when the 2B scheme is used [5,7]. Good VLE results are obtained for mixtures of alcohols with alkanes as well as for cross-associating systems, often better than those when all SAFT parameters are fitted to vapor pressures and liquid densities, but in some case using additional properties (than vapor pressures and liquid densities) in the parameter estimation yields improved pure compound parameters in association equations of state [7].…”
Section: Methanol and Ethanolmentioning
confidence: 99%
“…Good VLE results are obtained for mixtures of alcohols with alkanes as well as for cross-associating systems, often better than those when all SAFT parameters are fitted to vapor pressures and liquid densities, but in some case using additional properties (than vapor pressures and liquid densities) in the parameter estimation yields improved pure compound parameters in association equations of state [7]. It is concluded from these investigations that it is possible using quantum chemistry to eliminate one of the two association parameters of SAFT, but typically not both [2,15]. The remaining parameters must be fitted to vapor pressure and liquid density data.…”
Section: Methanol and Ethanolmentioning
confidence: 99%