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90                                                       Chapter 3


                 We  can  write  a  similar  relationship  for propane.  One  equilibrium relation-
            ship can be written for each component in a mixture.

            System Properties

            After  writing mass balances, energy balances,  and equilibrium relations, we need
            system property data to complete the formulation of the problem.  Here, we divide
            the system property  data  into thermodynamic, transport, transfer,  reaction proper-
            ties, and economic data.  Examples of thermodynamic properties are heat capacity,
            vapor pressure,  and  latent heat  of  vaporization.  Transport properties  include vis-
            cosity, thermal  conductivity,  and  diffusivity.  Corresponding  to  transport proper-
            ties are the transfer  coefficients,  which are friction  factor  and heat and mass trans-
            fer  coefficients.  Chemical  reaction properties  are  the  reaction  rate  constant  and
            activation  energy. Finally,  economic  data  are equipment  costs, utility costs,  infla-
            tion index, and other data, which were discussed in Chapter 2.
                 There frequently  seems to be insufficient  system property data. We may ob-
            tain  accurate  system property  data  from  laboratory  measurements,  which  are  ex-
            pensive. To avoid making measurements, we must rely on correlations or empiri-
            cal equations for estimating these data. Reid et al.  [2] have compiled many useful
            methods  for estimating  thermodynamic  as  well  as  transport  properties.  In  most
            cases, these methods are empirical or at best semi-empirical with limited accuracy.
            The accuracy of  system property data may limit the accuracy of process calcula-
            tions. Without  experimental  data,  we can attempt to  estimate  the thermodynamic
            property from a knowledge of the molecular structure of a molecule.  For example,
            if we know the molecular  structure  of a pure organic compound, its heat capacity
            may be estimated by adding the contribution to the heat capacity made by various
            functional  groups,  such as —CH 3, —OH, —O—, etc.,  as illustrated by Reid et al.
            [2]. We can estimate other properties by these "group methods."  An ultimate goal
            of  physical  property  research  is  to  be  able  to  calculate  accurately  any  physical
            property of a compound  from  its basic molecular properties. Thus, we can reduce
            the need for costly property measurements.
                 Temperature  and  composition  affect  physical  properties,  but  the  effect  of
            pressure is generally small and we can neglect it. One exception is gas density.  A
            well known example of the  effect  of temperature  is the  variation  of heat capacity
            of a gas with temperature, which is generally curve fitted  in the  form of a polyno-
            mial.

                         2
            Cp = a + bT  + cT  + dT 3                                  (3.16)
                An equation of  state  describes the variation of molar  density of a gas with
            pressure  and  temperature.  For  a  gas  at  high  temperature  and  low  pressure,  the
            ideal gas law,
            p = P/RT                                                   (3.17)




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