Page 123 - Petroleum and Gas Field Processing
P. 123

Figure 32 Material balance for flash vessel.


                  Functional form:

                            i¼c
                                     Z i
                            X
                      f ðgÞ¼                   1                         ð30Þ
                                1   gð1   K i Þ
                            i¼1
                     where g ¼ V/F. The desired root to this function, gr ¼ (V/F)r,is
                     the value that makes the function f(g) goes to zero or the sum of
                     [X i ] ¼ 1. The solution of this flash equation is carried out using
                     computers. Details on using functional technique are fully
                     described in Ref. 9.
            The vapor–liquid equilibrium constant, defined as


                 K i ¼ Y i =X i
            where Y i is the mole fraction of component i in the vapor phase, X i is the
            mole fraction of component i in the liquid phase, and K i is the equilibrium
            constant of component i for a given T and P, is considered the key
            concept used in the computation of phase behavior of hydrocarbon
            mixtures in oil and gas streams. K is called the distribution constant
            because it predicts the distribution of a component in each phase: vapor
            and liquid.






 Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
   118   119   120   121   122   123   124   125   126   127   128