bethw
Mechanical
- Sep 29, 2003
- 39
Our plant has a DA that is maintained at 5 lbs. It is supplied by steam from a prv. The steam pressure before the prv is 85 lbs. If I remember my basic thermo right, because this steam comes through a prv, it is superheated when it is reduced to the 5 lbs. Using what I remember about the adiabatic throttling process, the temperature of this steam after the prv should be around 290 degF, in a perfect world. So the steam entering the DA should be at about the same temp, right? So why is the temp of the DA and the condensate leaving it only at the saturation temp of 5 lbs (about 230F)? Has the "extra" enthalpy gone into the water requiring less steam usage?