dabigoj
Mechanical
- Sep 23, 2009
- 4
I am trying to determine the temperature of the steam after it goes through a pressure reducing valve (prv).
The upstream pressure is 600 psig @ saturation temperature. The down stream pressure is 400 psig.
From my understanding going through a prv the enthalpy of the system should stay the same.
Therefore, I usually look up the enthalpy at the higher pressure then look up the properties of the steam with the lower pressure and same enthalpy. Thus I get the down stream temperature. For the case above the enthaply at saturation temperature are listed below.
Enthalpy of saturated 600 psig steam is 1203.50 btu/lb
Enthalpy of saturated 400 psig steam is 1205.16 btu/lb
Therefor my method does not work to get the temperature or any properties of the lower pressure steam. Is there a more accurate way to calculate the down pressure steam?
The upstream pressure is 600 psig @ saturation temperature. The down stream pressure is 400 psig.
From my understanding going through a prv the enthalpy of the system should stay the same.
Therefore, I usually look up the enthalpy at the higher pressure then look up the properties of the steam with the lower pressure and same enthalpy. Thus I get the down stream temperature. For the case above the enthaply at saturation temperature are listed below.
Enthalpy of saturated 600 psig steam is 1203.50 btu/lb
Enthalpy of saturated 400 psig steam is 1205.16 btu/lb
Therefor my method does not work to get the temperature or any properties of the lower pressure steam. Is there a more accurate way to calculate the down pressure steam?