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Process Circuit Analysis                                      123


                 After  counting all the  equations and variables in Tables 3.4.1  and 3.4.2, we
            find  that we now have zero degrees of  freedom.  Thus, we have defined  the prob-
            lem,  and  we  can now  outline  the  solution procedure.  The  twenty-two  equations
            are decoupled, i.e., it is not necessary to solve all them simultaneously.  By inspec-
            tion  we  find  that  we  can  solve  the  mole  balance  equations  independently  of  the
            energy balance.  This frequently  occurs, usually when the temperatures in some of
            the lines are known.  Furthermore, in this case, we do require an iterative calcula-
            tion  procedure.  We  again  obtained  a  solution  procedure by  inspection,  which  is
            given in Table 3.4.3.
                 Frequently,  we  do  not  analyze  simple  process  problems  by  the  approach
            given in Tables 3.4.1 to 3.4.3. Instead, from the beginning, we assume that a solu-
            tion  is  possible,  and  we  carry  out  the  calculations,  introducing  equations  as
            needed.  With experience one  can recognize that certain problems have solutions,
            however, in most cases it is not evident that there is enough information to solve a
            problem, particularly when the solution contains many equations.  In this problem,
            we  will  calculate  the  mole  balance  quickly  without  a  formal  analysis,  once  we
            know that the degrees of freedom are zero.
                 Because there  is  1000 kmol/h  (2204  Ib mol/h)  of  methanol  in  line  3,  there
            will be 200 kmol/h (440.8 Ib mol/h) of methanol and 800 kmol/h of formaldehyde
            in line 4 because the conversion is 80 %. If 80 % of the stoichiometric quantity of
            oxygen is required, there will be 0.8 (1/2) (1000) = 400 kmol/h (881.6 Ib mol/h) of
            oxygen at lines 2 and 3 and zero at line 4. The nitrogen flow rate in lines 2, 3 and 4
            is (0.79/0.21) (400) =  1505 kmol/h (3317 Ib mol/h). It is good practice to tabulate


            Table 3.4.2  Summary of Equations for a Mixer_______________

            Mole Balances


            m I' = y3, 1m 3                                            (3.4.23)

            J2.2  m 2 = y 3, 2 m 3                                     (3.4.24)
            y2, 5'm 2=  y 3, 5m 3                                      (3.5.25)

            Variables

            Additional Variable is m 2.

            Degrees of Freedom

            F = 22 -  22 = 0






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