Page 187 - Standard Handbook Of Petroleum & Natural Gas Engineering
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172    General Engineering and Science




                                             CP      k  9 Cp/Cv      Acoustical
                                 Cas     Btu/(lbmole)   at 1 atm,   pa -  velocity at
                                            (OF)       60'F          6O0F,ft/sec
                              Air. . . . . . . . .   7.00   1.410   0.528   1,031
                              Helium.. . . .   4.968   1.66    0.486   2,840
                              Methane.. . .   8.44     1.308   0.545   1,350
                              Ethane.. . . .   12.30   1.193   0.565     967
                              Propane.. . .   17.10    1.133   0.577     793
                              Isobutane. ..   22.4     1.097   0.585     68  1
                              n-Bucane.. .   23.0      1.094   0.585     680
                              0.6 gravity. .   8.84    1.299   0.546   1,309
                              0.7  gravity..   9.77    1.279   0.550   1,035




                                                  Table 2-9
                                        Values of Absolute Roughness,
                                       New, Clean, Commercial Pipes 111

                                                 e fr (0.3048 m)  x  IO6   Mable max
                                                                 variation off
                                Type of pipe or rubing   Range   Design  from design. 56
                                Asphalted ast iron   +oo    400    -st0  +I
                                Bras and copper     5         5    -st0  +5
                                Concrete        1.ooo   10.000   4.000   -35  to 50
                                Can iron           850      850   -1otu  +IS
                                Galvanizrd iron    500      SO0    Or0 +IO
                                Wrought  iron      1so       I IO   -5  to  10
                                Steel              I50       I so   -5  to  10
                                Rivctcd steel   3.000   30.000   6.000   -15  to 7s
                                Wood stave       600   3.000   2.000   -35  10 20
                                  Campiled fmm &e given  in 'Pipe  Friction  Manual.-  Hydnuli Inrrirur.  3d
                                ed..  1961.


                      The Reynolds number is the ratio of the inertia forces acting on the fluid to the
                    viscous forces acting on the fluid. It is dimensionless and may be calculated as


                                                                                  (2-56)
                      The term p in Equation 2-56 is the dynamic viscosity of the fluid. The dynamic viscosity
                    is the ratio of the shear stress to the shear rate. It has units of (force  x time)/(area). The
                    most common unit of viscosity is the centipoise (1 centipoise = 0.01 g/cm - s). Dynamic
                    viscosity may be a function of temperature, pressure, and shear rate.
                      For Newtonian fluids the dynamic viscosity is constant (Equation 2-57), for power-
                    law fluids the dynamic viscosity varies with shear rate (Equation 2-58), and for Bingham
                    plastic fluids flow occurs only after some minimum shear stress, called the yield stress,
                    is imposed (Equation 2-59).
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