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Temperature of Steam After it goes through a PRV 1

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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?
 
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The enthalpy of the system (in theory) stays the same. Some of the steam will condense.
 
Goober Dave,

Thanks for the link, but that is what I use to get my properties. The problem is if I put in 400 psig with 1203.5 BTU i get an error.
 
MisterDonut,

Thanks, so if i understand correctly the 400 psig steam will just be at saturation temperature?

OJ
 
The steam will be at 400 psig but it will be "wet," meaning a mixture of saturated steam and saturated liquid.
 
If the 600# steam is at saturation is is about 488*f. When you reduce the pressure you are not reducing the temperature so the 400# steam should be slightly superheated still around 488*f. Unless you desuperheat it it will remain hotter than saturation. Another point to ponder if enthalpy is btu/lb than the more the lbs or psi the more the btu's??
 
dabigoj - correct. There is an inflection point at about 460 psia.

Good luck,
Latexman

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Forget what I just said. Damn I wish I could delete my post. Should have thought it through before posting. Right out of uni. My bad.
 
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