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Amount of flash steam, DN behind trap
Condensate flowrate:
kg/h
Pressure upstream of steam trap P1:
bar(a)
Pressure downstream of steam trap P2:
bar(a)
Condensate undercooling:
K
Possible savings when reusing flash steam (optional)
Steam price in local currency per ton:
t
Plant operation: Hours per day:
d
Plant operation: Days per year:
h
Condensate undercooling:
kJ/kg
Heat of evaporation at P2:
kJ/kg
Enthalpy of boiling condensate at P1:
kJ/kg
Enthalpy of boiling condensate at P2:
kJ/kg
Enthalpy of undercooled condensate at P2:
kJ/kg
Amount of flash steam:
kg/h
Amount of flash steam:
%
Specific steam volume at P2:
m³/kg
Flash steam volume:
m³/h
DN behind steam trap at 20 m/s:
mm
Possible savings in local currency per year:
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