Page 407 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
P. 407

simulation  in  terms  of  an  output  report.  Often,  graphical  displays  of  tower  profiles,  heating
                                curves, and a variety of other useful process data can be produced.
                          6.   Flowsheet Solver: This portion of the simulator controls the sequence of the calculations and the
                                overall convergence of the simulation.


                    Figure 13.1 Relationship between Basic Computational Elements and Required Input to Solve a Process
                    Simulation Problem









































                    There are several other elements commonly found in process simulators that are not shown in Figure 13.1.
                    For example, there are file control options, the option to use different engineering units, possibly some
                    additional features associated with regressing data for thermodynamic models, and so on. The availability
                    of these other options is dependent on the simulator used and will not be discussed further.


                    Also shown on the right-hand side of the diagram in Figure 13.1 are the seven general steps to setting up a
                    process simulation problem. The general sequence of events that a user should follow in order to set up a
                    problem on a simulator is as follows:
                          1.      Select  all  of  the  chemical  components  that  are  required  in  the  process  from  the  component
                                database.
                          2.      Select  the  thermodynamic  models  required  for  the  simulation.  These  may  be  different  for
                                different pieces of equipment. For example, to simulate correctly a liquid-liquid extractor, it is

                                necessary to use a thermodynamic model that can predict liquid-phase activity coefficients and
                                the  existence  of  two  liquid  phases.  However,  for  a  pump  in  the  same  process,  a  less
                                sophisticated model could be used.
                          3.   Select the topology of the flowsheet to be simulated by specifying the input and output streams
                                for each piece of equipment.
                          4.   Select the properties (temperature, pressure, flowrate, vapor fraction, and composition) of the
                                feed streams to the process.
   402   403   404   405   406   407   408   409   410   411   412