= 1.7
pd > pu / 2:
Kv = 0.032 m (vd / (pu - pd))1/2 (2)
where
m = mass flow (kg/h)
pu = upstream pressure (bar abs)
pd = downstream pressure (bar abs)
vd = specific weight of downstream steam and actual temperature (m3/kg)
pd < pu / 2:
Kv = 0.032 m (2 vd2 / pu )1/2 (2b)
where
vd2 = specific volume for steam with pressure pu / 2 and actual temperature (m3/kg)
pd > pu / 2:
Kv = 0.0019 q (ρg Tu / (pd (pu - pd)))1/2 (3)
where
q = volume flow of gas at 0oC and 1013 mbar (m3/h)
ρg = density of gas at 0oC and 1013 mbar (kg/m3)
Tu = upstream temperature (K)
pu = upstream pressure (bar abs)
pd = downstream pressure (bar abs)
pd < pu / 2:
Kv = 0.0039 q (ρg Tu)1/2 / pu (3b)
Control Valve terminology, bodies, trim, flow characteristics, Cv and Kv sizing, noise, actuators and positioners
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Sizing of water control valves - SI units
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