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Mixture Corresponding-States Relations

Differentiation of the mixing rules with respect to temperature, T, yields [Pg.160]

In order to perform phase-equilibrium calculations, fugacity coefficients can be calculated from the thermodynamic relationship [Pg.161]


As shown in Section II.D(2), the determinant of Eq. III.133 can be brought to correspond to a pure spin state by imposing a certain condition (11.61) on the relation between p+ and p. which corresponds to the pairing of the electrons. If p+ and p are permitted to vary independently of each other, the determinant is no longer a pure spin state but a mixture of states associated with the quantum numbers... [Pg.308]

The Law of Corresponding States has been extended to cover mixtures of gases which are closely related. As was brought out in Chapter 2, obtaining the critical point for multicomponent mixtures is somewhat difficult therefore, pseudocritical temperature and pseudocritical pressure have been invented. [Pg.111]

Related Calculations. This illustration outlines various simple techniques for estimating P-V-T properties of gaseous mixtures. Obtain the compressibility factor from the generalized corresponding-state correlation, as shown in step 2. [Pg.12]

Once this function is determined, it could be applied to any substance, provided its critical constants Pc, T, and V are known. One way of applying this principle is to choose a reference substance for which accurate PVT data are available. The properties of other substances are then related to it, based on the assumption of comparable reduced properties. This straightforward application of the principle is valid for components having similar chemical structure. In order to broaden its applicability to disparate substances, additional characterizing parameters have been introduced, such as shape factors, the acentric factor, and the critical compressibility factor. Another difficulty that must be overcome before the principle of corresponding states can successfully be applied to real fluids is the handling of mixtures. The problem concerns the definitions of Pq P(> and Vc for a mixture. It is evident that mixing rules of some sort need to be formulated. One method that is commonly used follows the Kay s rules (Kay, 1936), which define mixture pseudocritical constants in terms of constituent component critical constants ... [Pg.13]

An extension of corresponding states to highly polar substances has been based on the acentric factor correlation. A fourth parameter related to the dipole moment must be introduced. A similar four-parameter description of the virial coefficients of polar fluids and their mixtures has been developed by Halm and Stiel and for mixtures of quadrupolar fluids by Ramaiah and Stiel. ... [Pg.218]

Relation Between Gaseous and Liquid Mixtures.—As we have indicated, second virial coefficients can be calculated by corresponding-states methods with sufficient accuracy to be useful in predicting the properties of pure gaseous substances and their mixtures. This is of considerable practical importance for... [Pg.220]

The multi-fluid approach can always be used with corresponding states methods for well-defined mixtures. In the one-fluid approach, however, a mixing rule must be proposed for each of the input parameters. For the Petersen et al. [22] corresponding states model discussed earlier, the following relations [31] are used to extend the model to mixtures ... [Pg.15]

Flory et al. [76—78] developed a theory which relates the thermodynamic behaviour of solutions to the structure and molecular forces of single components and which improves the agreement with experimental data [79]. They employed for mixture a partition function such that the influence of single component structural characteristics is preserved. The new theory combines some features of the corresponding state theory [4] with others of cell theory [4] and avoids some deficiences of both types of theory. [Pg.69]

During the mid-1970s, researchers at the National Institute of Standards and Technology (NIST) at Boulder, Colorado undertook a series of projects with the objectives of measuring and predicting the properties of liquefied natural gas and related mixtures. One result from this project was an extended corresponding-states model for liquefied natural gas densities developed by McCarty. That implementation used a 32-term, modified Benedict-Webb-Rubin equation of state for methane as the reference fluid and shape factors which had the same functional form as those proposed by Leach, but which had been re-fit to liquefied natural gas density data. The model reproduced the available liquefied natural gas density data to within 0.1 %. Eaton et alP used McCarty s methane equation to predict critical lines and VLB in (methane ethane). [Pg.163]

Corresponding states are found with shape factors, and 6, that relate the reduced properties of the mixture to those of the reference fluid. The thermodynamic properties for the mixture are reduced by the pseudo-critical parameters pc,x and defined by... [Pg.425]

Representation of mixtures is based on the one-fluid corresponding-states principle. Two steps are required to represent a mixture the mixture is first characterized as a hypothetical pure fluid and then the resulting hypothetical pure fluid is related to the reference fluid using equations (12.1) and (12.6). The mixing rules are... [Pg.285]

This relation expresses the critical temperature of the mixture in terms of intermolecular forces and of the properties of a reference system which may be either the mixture treated in the approximation of the conformal solutions or any single component which satisfies the theorem of corresponding states. [Pg.245]

A proper resolution of Che status of Che stoichiometric relations in the theory of steady states of catalyst pellets would be very desirable. Stewart s argument and the other fragmentary results presently available suggest they may always be satisfied for a single reaction when the boundary conditions correspond Co a uniform environment with no mass transfer resistance at the surface, regardless of the number of substances in Che mixture, the shape of the pellet, or the particular flux model used. However, this is no more than informed and perhaps wishful speculation. [Pg.149]


See other pages where Mixture Corresponding-States Relations is mentioned: [Pg.160]    [Pg.160]    [Pg.154]    [Pg.76]    [Pg.125]    [Pg.129]    [Pg.15]    [Pg.47]    [Pg.54]    [Pg.174]    [Pg.216]    [Pg.155]    [Pg.226]    [Pg.226]    [Pg.155]    [Pg.7]    [Pg.304]    [Pg.160]    [Pg.30]    [Pg.217]    [Pg.15]    [Pg.349]    [Pg.1265]    [Pg.169]    [Pg.202]    [Pg.175]    [Pg.33]    [Pg.645]    [Pg.268]    [Pg.181]    [Pg.25]    [Pg.46]    [Pg.146]    [Pg.589]    [Pg.608]    [Pg.351]   


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