1962
DOI: 10.1002/aic.690080412
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Prediction of vapor‐liquid equilibria from the corresponding states principle

Abstract: A new ideal K value is defined which does not depend on the Lewis and Randall ideal solution rule but is derived only from composition dependent pseudo criticals and the corresponding states principle. Properties of the liquid and vapor mixtures are evaluated from either experimentally measured properties of closely related pure substances or from generalized tables of thermodynamic properties. A derivation of an improved pseudocritical expression applicable to liquids which may be approximated by simple spher… Show more

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Cited by 78 publications
(39 citation statements)
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“…The comparisons are shown in terms of deviations (δx) of the solubilities (liquid mole fraction nitrogen) from values predicted using the PR EOS, using temperature independent C ij and D ij values determined from the present data. 8 The figure facilitates a sensitive analysis of differences in data sets. The difference in the deviations between data sets (not the magnitude of the deviation of either set from the reference EOS model) is of interest in these data comparisons.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…The comparisons are shown in terms of deviations (δx) of the solubilities (liquid mole fraction nitrogen) from values predicted using the PR EOS, using temperature independent C ij and D ij values determined from the present data. 8 The figure facilitates a sensitive analysis of differences in data sets. The difference in the deviations between data sets (not the magnitude of the deviation of either set from the reference EOS model) is of interest in these data comparisons.…”
Section: Resultsmentioning
confidence: 99%
“…Figure 1. The one-fluid approach, introduced by van der Waals, is the most commonly used method for extending equations of state to nonpolar mixtures (8). This approach assumes that the properties of a mixture are equivalent to those of a hypothetical pure component at the same temperature and pressure, with the characteristic constants properly averaged over the composition (8).…”
Section: Resultsmentioning
confidence: 99%
“…2. To correct for this deficiency we use the mean density approximation (Leland et al, 1962;Mansoori and Leland, 1972) of the pair correlation function which is known to be accurate in representing the dependence of the pair correlation function on the energy parameter (Hoheisel and Lucas, 1984). The mean density approximation assumes the following: g12@/~12?…”
Section: Approximations and Discussionmentioning
confidence: 99%
“…It can be justified empirically for van der Waals fluid mixtures whenever the a and b terms for the mixture are given by the empirical P 8 x*xjulj and P 8 XIXjbzj. In this case van der Waals equation can be rearranged as follows in the form of Equation (13) after the distribution functions have been approximated by (15) and (16) :…”
Section: P N T ) 4 R R L ? D R T Jmentioning
confidence: 99%
“…This assumption in Equations (15) and (16) considerably modifies the dependence of the radial distribution function on composition. I t assumes that in addition to r and T the distribution function is dependent only on the force parameters of the molecules in the pair and the average reduced density of the mixture around the pair.…”
Section: P N T ) 4 R R L ? D R T Jmentioning
confidence: 99%