Page 411 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
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simulation. The transport and other properties are used in equipment sizing calculations. The techniques
                    used  in  the  simulators  are  no  more  accurate  than  those  covered  in  transport,  thermodynamics,  unit
                    operations, and separations courses—they are just easier to apply.


                    Even  though  simple  mass  and  energy  balances  cannot  be  done  by  the  simulator  without  the  above-
                    mentioned pure-component properties, often the most influential decision in a simulation is the choice of a
                    model to predict phase equilibria. Several of the popular simulators have expert systems to help the user
                    select  the  appropriate  model  for  the  system.  The  expert  system  determines  the  range  (usually  with
                    additional user input) of operating temperatures and pressures covered by the simulation and, with data on
                    the components to be used, makes an informed guess of the thermodynamic models that will be best for the
                    process being simulated. The word expert should not be taken too seriously! The expert-system choice is
                    only a first guess. Additionally, the model chosen may not be best for a given piece of equipment. A
                    moderately complex simulation will use at least two different thermodynamic packages for different parts
                    of the flowsheet.


                    Due to the importance of thermodynamic model selection and the many problems that the wrong selection
                    leads to, a separate section (Section 13.4) is dedicated to this subject. An example of how the wrong

                    thermodynamic package can cause serious errors is given in Example 13.1.

                    Example 13.1



                    Consider the HCl absorber (T-602) in the separation section of the allyl chloride process, Figure  C.3
                    (Appendix C, on the CD). This equipment is shown in Figure E13.1. The function of the absorber is to
                    contact  countercurrently  Stream  10a,  containing  mainly  propylene  and  hydrogen  chloride,  with  water,
                    Stream  11.  The  HCl  is  highly  soluble  in  water  and  is  almost  completely  absorbed  to  form  32  wt%
                    hydrochloric  acid,  Stream  12.  The  gas  leaving  the  top  of  the  absorber,  Stream  13,  is  almost  pure
                    propylene, which is cleaned and then recycled.


                    Figure E13.1 HCl Absorber in Allyl Chloride Separation Section (Unit 600), Appendix C
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