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The simplest form of the virial equation has validity only at low to moderate pressures where Z is linear in pressure The generalized virial-coefficient correlation is therefore useful only where Z0 and 2' are at least approximately linear functions of reduced pressure Figure 315 compares the linear relation of Z0 to P, as given by Eqs (360) and (361) with values of Z0 from the LeeIKesler compressibility-factor correlation, Tables E1 and E3 The two correlations differ by less than 2% in the region above the dashed line of the figure For reduced temperatures greater than T, x 3, there appears to be no limitation on the pressure For lower values of T, the allowable pressure range decreases with decreasing temperature A point is reached, however, at T, x 07 where the pressure range is limited by the saturation pressure17



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1 6 ~ h e scorrelations first appeared in 1975 in the third edition of this book, attributed as a personal communication e to M M Abbott, who developed them 17~lthough LeeIKesler tables, App E, list values for superheated vapor and subcooled liquid, they do not provide the values at saturation conditions

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This is indicated by the left-most segment of the dashed line The minor contributions of 2' to the correlations are here neglected In view of the uncertainty associated with any generalized correlation, deviations of no more than 2% in 2 are not significant ' The relative simplicity of the generalized virial-coefficient correlation does much to recommend it Moreover, temperatures and pressures of many chemical-processing operations lie within the region where it does not deviate by a significant amount from the compressibilityfactor correlation Like the parent correlation, it is most accurate for nonpolar species and least accurate for highly polar and associating molecules The question often arises as to when the ideal-gas equation may be used as a reasonable approximation to reality Figure 316 can serve as a guide

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The next step building a full package on your old release and deploying it to a workstation that will not be used prior to the upgrade or update should be considered a safety stop If you have a problem with an object, you can then recover the object by checking it in from this client workstation, which is a lot easier than recovering a full set of central object tables from tape for one object! To do this, you would need to leverage your save location to restore an object (If you do not have a save location, consider setting one up Detailed instructions for configuring a save location can be found on the wwwpeoplesoftcom web site) To do this, you would save the object to the save location from the workstation, check out the object onto the workstation (overlaying the local specs), restore the object from the save location (overlaying the local specs with the original objects), and then check the object back in The object would now be back to the same state it was in before you started the update Again, this last step is a valuable safety check, and we would not recommend skipping it DEFINITION Restore from a save location: This is the process of using the save location to allow you to restore an object s previous state and check it back into central objects This procedure should only be used when necessary, as you are replacing what is in your central objects with what is on the client workstation

Determine the molar volume of n-butane at 510K and 25bar by each of the following: (a) The ideal-gas equation

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Although the molar volumes of liquids can be calculated by means of generalized cubic equations of state, the results are often not of high accuracy However, the LeeIKesler correlation includes data for subcooled liquids, and Fig 314 illustrates curves for both liquids and gases Values for both phases are provided in Tables El through E4 Recall, however, that this correlation is most suitable for nonpolar and slightly polar fluids In addition, generalized equations are available for the estimation of molar volumes of saturated liquids The simplest equation, proposed by ~ackett,"is an example:

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