Page 238 - Modelling in Transport Phenomena A Conceptual Approach
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218         CHAPTER 7.  UNSTEADY-STATE MACROSCOPIC BALANCES


             L         length,  m
             m         mass flow rate,  kg/s
             M         molecular weight,  kg/ kmol
             n         molar flow rate,  kmol/s
             P         pressure,  Pa
             Q         heat transfer rate,  W
             Q         volumetric flow rate,  m3/ s
             r         rate of a chemical reaction,  kmol/ m3. s
             R         gas constant,  J/mol. K
             T         temperature,  "Cor K
             t         time,  s
             U         internal energy, J
             V         volume,  m3
             V         velocity,  m/ s
             w         rate of  work, W
             ws        rate of  shaft work,  W
             X         fractional conversion
             Xi        mole fraction of  species i
             CY        thermal diffusivity, m2/ s
                       stoichiometric coefficient of  ith species in the jth reaction
             "ij
             Y         CP/G
             A         difference
             AH,,,     heat of  reaction,  J
             E         molar extent of a reaction,  kmol
             x         latent heat,  J
                                                                     s
             U         kinematic viscosity (or, momentum diffusivity), m2/
             P         density, kg/ m3
             7         residence time,  s
            Overlines

                        per mole
             N
                        per unit mass
             -          partial molar

            Bracket

             (4         average value of a

            Superscripts

             0          standard state
             S          solid
             sat        saturation
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