Vapor-Liquid Equilibrium Calculations Using K Values

where yA = mole fraction of A in the vapor phase and xA = mole fraction of A in the liquid phase. For light hydrocarbon systems (methane to decane), the K values have been determined semi-emperically and can be evaluated from the equations given in Table 3.13. In general, K is a function of temperature, pressure, and composition. Table 3.1. ................
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