Page 62 - Process simulation and control using Aspen
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ASPEN PLUS    SIMULATION OF REACTOR MODELS         55

        2 .2  ASPEN PLUS SIMULATION OF A RStolc MODEL


         Problem statement
        Styrene is produced by dehydrogenation of ethylbenzene. Here we consider an
         irreversible reaction given as:

                                 CgHs-C2H5 -> CgHs-CH - CH2 + H2
                                ethylbenzene   styrene     hydrogen

         Pure ethylbenzene enters the RStoic reactor with a flow rate of 100 kmol/hr at 260oC
         and 1.5 bar. The reactor operates at 250 oC and 1.2 bar. We can use the fractional
        conversion of ethylbenzene equals 0.8. Using the Peng-Robinson thermodynamic method,
        simulate the reactor model.

         Simulation approach
        As we start Aspen Plus from the Start menu or by double-clicking the Aspen Plus icon
        on our desktop, first the Aspen Plus Startup dialog appears (see Figure 2.1). Choose
         Template option and then click OK.



                  iaj _1_J __J *j rv.Mft, I-Hid 3  I I l-J±]-J _J



















                                            _ J











                                              FIGURE 2.1
            As the next window pops up (see Figure 2.2), select General with Metric Units and
         hit OK button.


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