2013
DOI: 10.1016/j.fluid.2013.04.003
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An improved Helmholtz energy model for non-polar fluids and their mixtures. Part 1: Application to non-polar pure fluids

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Cited by 6 publications
(7 citation statements)
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References 282 publications
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“…On the one hand, the mixture model could readily meet the above requirement on the extension to more fluids because of its formulation as an extended corresponding states (ECS) model. Indeed, in the work of [1] coefficients were reported for ethylene, benzene and toluene, which are fluids that Kunz et al [4] reported to be further incorporated into the GERG-2004 equation. On the other hand, and more importantly, it was shown in [2] that the mixture model meets the requirements on accuracy of the current multi-fluid mixture models [9].…”
Section: Introductionmentioning
confidence: 94%
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“…On the one hand, the mixture model could readily meet the above requirement on the extension to more fluids because of its formulation as an extended corresponding states (ECS) model. Indeed, in the work of [1] coefficients were reported for ethylene, benzene and toluene, which are fluids that Kunz et al [4] reported to be further incorporated into the GERG-2004 equation. On the other hand, and more importantly, it was shown in [2] that the mixture model meets the requirements on accuracy of the current multi-fluid mixture models [9].…”
Section: Introductionmentioning
confidence: 94%
“…The calculation of caloric properties requires the perfect-gas isochoric heat capacity, c pg V,m . To that effect, a variety of correlations for c pg V,m /R were used in the work of [1], which were reproduced here for convenience. The following ancillary equations associated with reference equations of state were used: Setzmann and Wagner [12] for methane, Span et al [14] for nitrogen, Span and Wagner [15] for carbon dioxide and Stewart et al [16] for oxygen.…”
Section: Fundamentals Of the Proposed Modelmentioning
confidence: 99%
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