Page 271 - Valve Selection Handbook
P. 271

258                   Valve Selection  Handbook

                                   Table 7-1.  (continued)
                                      Nomenclature
                                                   Mixed SI     Mixed US
                                                   Units        Units
              f    Pipe friction  factor = number
                   of velocity heads lost in length
                   of pipe equal to diameter
              F    Gas flow constant for subsonic
                   nozzle flow,  based on isentropic
                   coefficient  k at standard conditions
                   and the absolute pressure ratio
                   across the valve
                   Discharge reactive  force         N            Ib
              F d
              g    Gravitational acceleration        9.807 m/sec 2  32.174  ft/sec 2
                   Proportionality constant          l.Okgm/Ns 2  32.174
              g c
                                                                  lb mft/lb fs 2
              G    Specific gravity of the liquid referred
                   to water =  1.00 at 70°F (20°C)
              k    Isentropic coefficient
              K    Derated or certified coefficient
                   of discharge 1
                   Capacity correction factor accounting
              K b
                   for  the effect  of built-up and  superimposed
                   back pressure on valve lift  of bellows
                   balanced pressure  relief  valves
                   Actual coefficient  of discharge 2
             K d
                   Napier capacity correction factor
             K N
                   for  pressure
                   Napier capacity correction  factor for
             K SH
                   superheat
                   Velocity head loss of rupture devices
             K R
                   Viscosity correction factor
             K v
             1     Length of pipeline                mm           in.
             M     Molecular weight                  kg/kmol      Ib/lbmol
                                                                     2
             P     Set pressure (gauge)              barg         Ib/in g
             PI    Relieving pressure (gauge) = set
                   pressure plus overpressure plus
                                                                     2
                   atmospheric pressure             bara          Ib/in a
                                                                     2
             Po    Pressure  at valve outlet        bara          Ib/in a
            1
              ASME (1992) Section VIII Division, UG-131(e)(3)
            2
              ASME (1992) Section VIII Division, UG-131(e)(2)
   266   267   268   269   270   271   272   273   274   275   276