Kamakal
Chemical
- May 20, 2005
- 8
Hello:
I have an exchanger using steam as a heating medium. Steam pressure inside the exchanger is 600# psig. Steam trap outlet goes to a drum 300 feet away operating at 70 psig. Does it mean that the pressure drop is consumed by the trap or by the line and exit losses.
I am designing a PSV for the drum considering a case of fail open steam trap. The trap condensate line is 3". If I use the Cv value for a 3" open gate, is it reasonable that I get a steam load for the PSV?
Thanks for your replies in advance.
Kamakkal
I have an exchanger using steam as a heating medium. Steam pressure inside the exchanger is 600# psig. Steam trap outlet goes to a drum 300 feet away operating at 70 psig. Does it mean that the pressure drop is consumed by the trap or by the line and exit losses.
I am designing a PSV for the drum considering a case of fail open steam trap. The trap condensate line is 3". If I use the Cv value for a 3" open gate, is it reasonable that I get a steam load for the PSV?
Thanks for your replies in advance.
Kamakkal