Sherifhosny
Industrial
- Jan 13, 2020
- 15
Good morning
I was asked to make the selection of two steam traps after a heat exchanger.
what I see in the PID ( in the attachment) is that they use two steam traps, one of them is the normal one and the other is for the start-up. is the start-up one needed here, given that it is a condensate line?
also, should the capacity for this steam trap be the same mass flow rate of the heat exchanger? and what is the normally allowable pressure drop over the trap?
I am handling steam traps for the first time so any information even the simplest one would be valuable.
I was asked to make the selection of two steam traps after a heat exchanger.
what I see in the PID ( in the attachment) is that they use two steam traps, one of them is the normal one and the other is for the start-up. is the start-up one needed here, given that it is a condensate line?
also, should the capacity for this steam trap be the same mass flow rate of the heat exchanger? and what is the normally allowable pressure drop over the trap?
I am handling steam traps for the first time so any information even the simplest one would be valuable.