Page 273 - Pipeline Rules of Thumb Handbook
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260     Pipeline Rules of Thumb Handbook

         where d = density, g-moles/l                                          Transport properties

                                                                 Viscosity (liquid) 2
                            4
         in which the constants for methane are:
                                                                 t°C                          m, centipoises
         B o = 0.042600
                                                               -185                           0.226 (subcooled)
         A o = 1.85500                                         -180                           0.188
                                                               -175                           0.161
         C o = 22,570.0                                        -170                           0.142
                                                               -165                           0.127
         b = 0.00338004
                                                               -160                           0.115 (at sat. pressure)
         a = 0.0494000
                                                                             7
                                                               Viscosity (vapor) at 1atm pressure:
         c = 2,545.00
                                                                 t°C                          m, centipoises
         g = 0.0060000
                                                               -181.6                         0.00348
         a = 0.000124359
                                                                -78.5                         0.00760
                                                                  0                           0.01026
         With these constants, R = 0.0820 liter-atm/(°K) (gram mole),  20                     0.01087
                                                                 100                          0.01331
         P is in atmospheres, T is in °K, and e is the base of natural
                                                                200.5                         0.01605
         logarithms. Constants in this equation are available for
                                                                 284                          0.01813
         ethane, ethylene, propane, propylene, n-butane, i-butane, i-  380                    0.02026
         butene, n-pentane, i-pentane, n-hexane, and n-heptane. 4
                                                                 499                          0.02264
         Using Equation 2 to predict the pressure corresponding to 89
         data points 5,6  it was found that the average absolute and  Additional data are available.
                                                                            8
         maximum deviations for methane were 0.376% and +2.25%
         respectively. Reference 6 discusses a generalization of the
         Benedict-Webb-Rubin equation.
                                                                           Thermal conductivity (liquid)

                                                                                   t°F               K, Btu/hrft°F
                                          2
                           Vapor pressure
                                                                                 -280             0.0841
                                        .
                                                .
             Freezing point in air at 1 atm =-296 46 ∞ F (182 48  ∞ C)  n.b.p.   -258.68          0.0790
                                                                                 -200             0.0568
                                        .
          Boiling point at 29.921-in. Hg =-258 68 ∞F           crit. temp        -115.8           0.029 (reference )
                                                                                                                10
                 ∞ )
               .
          - ( 161 49 C
                                                                 Values for liquid thermal conductivity represent estimates
                                                                                                      9
                                                               by the authors using the method of Viswanath which seems
         Vapor pressures are tabulated on p. 121 of Reference 2 from  to be quite reliable for organic liquids (halogenated com-
         10mm to 1,500mmHg and are represented by the Antoine  pounds excepted).
         equation.
                       (
                         +
             log 10 P =  A -  B C t)                     (3)              Thermal conductivity (vapor) 7
         or:                                                     t°F                                   K, Btu/hrft°F
                                                               -300                                    0.00541
               (
             t =  B A - log 10  P) -  C                  (3a)  -200                                    0.00895
                                                               -100                                    0.01265
                                                                -40                                    0.0149
         with P in mmHg and t in °C.
                                                                -20                                    0.0157
                                                                  0                                    0.01645
         A       = 6.61184                                       20                                    0.01725
         B       = 389.93                                        40                                    0.01805
         C       = 266.00                                        60                                    0.0190
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