sheiko
Chemical
- May 7, 2007
- 422
Hello,
I have a deaerator opened to atmosphere via 6-inch nozzle and operating at 0 barg.
The design pressure is 5 barg.
I have the following questions:
1/ Is the deaerator considered as a Pressure Vessel?
2/ Shall i check all the overpressure scenarii to determine if i need a safety relief valve?
Thank you
"We don't believe things because they are true, things are true because we believe them."
I have a deaerator opened to atmosphere via 6-inch nozzle and operating at 0 barg.
The design pressure is 5 barg.
I have the following questions:
1/ Is the deaerator considered as a Pressure Vessel?
2/ Shall i check all the overpressure scenarii to determine if i need a safety relief valve?
Thank you
"We don't believe things because they are true, things are true because we believe them."