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Process Circuit Analysis                                       117


                 After  substituting Equations 3.3.42 and 3.3.43 into Equation 3.3.39, and with
            some  algebraic  manipulation,  we  obtain  the  final  form  of  the  energy  equation,
            Equation 3.3.44.

                       yi,i         r       m 2V     (  m 2V  ^ 1
            I  ——————————————       I K 2>i h 2V, ; —— + h 2Lii 1 1 ——— |  |  -  h, = 0  (3.3.44)
              (K 2ji -  IHnWmO+l    L          raj  I    m l  j  J

                 The  calculation procedure  using  Equations  3.3.38  and 3.3.44  is outlined  in
            Table 3.3.4.
            Table 3.3.4:  Procedure for Calculating the Temperature of a
            Flashed Liquid _______________________________

                 1.  Calculate  the bubble-point  temperature.  Assume  a  temperature  and  then
            calculate values  for the  equilibrium relations from  Equations 3.3.22 and 3.3.23 in
            Table 3.2.2. Next, calculate the vapor-phase mole fractions  from Equations 3.3.20
            and  3.3.21.  Check  the results using  Equation  3.3.19.  Assume  a new temperature
            and repeat the calculation until  temperature converges to a desired degree of accu-
            racy.

            2.  Similarly, calculate the dew-point temperature. Assume a temperature and then
            calculate values for the equilibrium relations from  Equations  3.3.27 and  3.3.28 in
            Table  3.3.3.  Next,  calculate  the  liquid-phase  mole  fractions  from  3.3.25  and
            3.3.26.  Check  the results using  Equation 3.3.24.  Assume  a new temperature  and
            repeat the calculation until  temperature converges to a desired degree of accuracy.
            3. Assume a temperature, T 2,  between the bubble and dew point temperatures.

            4.  Calculate values  for  the  equilibrium relations  at T 2 from  Equations 3.3.8 and
            3.3.9  in Table 3.3.1.

            5.  Solve  for  the  mole  fractions  for  the  liquid  and  vapor  from  Equations  3.3.3,
            3.3.4, 3.3.6, and 3.3.7.


            6. Substitute these values into Equation 3.3.38 and solve for m 2V/m }  by trial.
            7.  Calculate  the pure-component  enthalpies  from  Equations  3.3.13  to  3.3.18  and
            the enthalpy of the feed solution from Equation 3.3.10.

            8.  Check  the guess  of T by  substituting  all  calculated  quantities  into  the  energy
                                2
            balance, Equation 3.3.44.
            9. Assume a new value of  T,  and repeat  steps 3 to 7 until the energy equation is
                                   2
            satisfied  within a sufficient  degree of accuracy.



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