A paucity of multicomponent liquid mixture thermal conductivities has left untested those thermal conductivity predictive models which are amenable to multicomponent mixtures. A transient hot-wire thermal conductivity cell was constructed, calibrated and used to measure ternary liquid mixture thermal conductivities over the entire composition range at 25°C and ambient pressure. These data were used to evaluate existing models which do not contain adjustable parameters. The Li model was found to be inadequate while the power-law model was found to be surprisingly accurate for nonaqueous systems, but it requires an adjustable parameter if water is one of the components. The local-composition model was found to agree well with the experiments without the above restriction. However, the agreement was even better if a new mixing rule is used, but the old rule should be retained for systems containing water. Ternary effects are unimportant and the local-composition model can be used for multi-component systems. Attempts to predict vapor-liquid equilibria from local compositions fitted from thermal conductivity data were unsuccessful.
%0 Journal Article
%1 citeulike:5003569
%A Rowley, Richard L.
%A White, Gary L.
%A Chiu, Mudau
%D 1988
%J Chemical Engineering Science
%K 82d15-liquids 80a20-heat-and-mass-transfer 82c70-transport-processes
%N 2
%P 361--371
%R 10.1016/0009-2509(88)85049-8
%T Ternary liquid mixture thermal conductivities
%U http://dx.doi.org/10.1016/0009-2509(88)85049-8
%V 43
%X A paucity of multicomponent liquid mixture thermal conductivities has left untested those thermal conductivity predictive models which are amenable to multicomponent mixtures. A transient hot-wire thermal conductivity cell was constructed, calibrated and used to measure ternary liquid mixture thermal conductivities over the entire composition range at 25°C and ambient pressure. These data were used to evaluate existing models which do not contain adjustable parameters. The Li model was found to be inadequate while the power-law model was found to be surprisingly accurate for nonaqueous systems, but it requires an adjustable parameter if water is one of the components. The local-composition model was found to agree well with the experiments without the above restriction. However, the agreement was even better if a new mixing rule is used, but the old rule should be retained for systems containing water. Ternary effects are unimportant and the local-composition model can be used for multi-component systems. Attempts to predict vapor-liquid equilibria from local compositions fitted from thermal conductivity data were unsuccessful.
@article{citeulike:5003569,
abstract = {{A paucity of multicomponent liquid mixture thermal conductivities has left untested those thermal conductivity predictive models which are amenable to multicomponent mixtures. A transient hot-wire thermal conductivity cell was constructed, calibrated and used to measure ternary liquid mixture thermal conductivities over the entire composition range at 25°C and ambient pressure. These data were used to evaluate existing models which do not contain adjustable parameters. The Li model was found to be inadequate while the power-law model was found to be surprisingly accurate for nonaqueous systems, but it requires an adjustable parameter if water is one of the components. The local-composition model was found to agree well with the experiments without the above restriction. However, the agreement was even better if a new mixing rule is used, but the old rule should be retained for systems containing water. Ternary effects are unimportant and the local-composition model can be used for multi-component systems. Attempts to predict vapor-liquid equilibria from local compositions fitted from thermal conductivity data were unsuccessful.}},
added-at = {2017-06-29T07:13:07.000+0200},
author = {Rowley, Richard L. and White, Gary L. and Chiu, Mudau},
biburl = {https://www.bibsonomy.org/bibtex/2fbd278bb4bb236427725d7d42739eb92/gdmcbain},
citeulike-article-id = {5003569},
citeulike-attachment-1 = {rowley_88_ternary_33847.pdf; /pdf/user/gdmcbain/article/5003569/33847/rowley_88_ternary_33847.pdf; 27f599cc5c0807386953363f5a663411adc2d3c7},
citeulike-linkout-0 = {http://dx.doi.org/10.1016/0009-2509(88)85049-8},
comment = {(private-note)circulated by SGM 2009-06-27},
doi = {10.1016/0009-2509(88)85049-8},
file = {rowley_88_ternary_33847.pdf},
interhash = {8ff0538c36243955379a45f107fe7e96},
intrahash = {fbd278bb4bb236427725d7d42739eb92},
issn = {00092509},
journal = {Chemical Engineering Science},
keywords = {82d15-liquids 80a20-heat-and-mass-transfer 82c70-transport-processes},
number = 2,
pages = {361--371},
posted-at = {2009-06-28 23:27:06},
priority = {2},
timestamp = {2019-11-07T23:04:54.000+0100},
title = {{Ternary liquid mixture thermal conductivities}},
url = {http://dx.doi.org/10.1016/0009-2509(88)85049-8},
volume = 43,
year = 1988
}