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Reactor Design                                                397


            Table 7.3.1  Reactor Composition


                       Component    Molecular    Reactor Composition
                                     Weight         Mole Fraction

                                                  Input      Output


                          H 2O        18.02      0.2861     0.30877
                                      16.04      0.4558     0.48139
                          CH 4
                                       2.0       0.0771     0.03730
                          H 2
                          CO          28.01      0.1140     0.00015
                                       44.0      0.1696     0.17253
                          C0 2
                     Temperature, K               527.6      588.7
                      Pressure, bar               27.92




            Source Ref.  27.
            Flow rate in              20,350 Ibmol/h (9230 kgmol/h)
            Superficial velocity      1 fl/s (0.3048 m/s)

                 Follow  the  procedure  outlined  in  Table  7.12  using  the  equations  listed  in
            Table 7.11.  First calculate the molar density  at 60 °F and  1 ami because the space
            velocity is given at standard conditions. From the ideal gas law,  the molar density
            at standard conditions,

                        1.01   1
                                                            3
                                                   3
                                                                   3
            Ps  —       ———   —— =   0.04204 kgmol/m  (2.63x10~  lbmol/ft )
                RT    0.08314  289
                 The volumetric flow rate at standard conditions,

                  9230
                                              6
                                    3
                                 5
            V vs = ———— = 2.196xl0  m /h  (7.75xl0  ftVh)
                 0.04204
                According to Equation 7.11.1,

                V vs  219600
                                     3
                                             3
            V B = —— = ————  = 73.20 m  (2580 ft ) of catalyst
                       3000
                 S cv

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