Hello all,
I have a DIB1 valve (10") that is used on a propane line; Propane's operating temperature is 150F and Operating pressure is 220 psia. At normal operating condition, propane is in vapor phase; However, in case of the valve closer, the temperature inside the valve cavity can fall below 110F (due to heat loss) and become liquid.
API 6D states:
"The manufacturer shall determine if the valve design could result in liquid being trapped in the body cavity in the open- and/or closed-valve position.
If liquid trapping is possible, the valve shall be provided with automatic cavity relief."
Now my question is that for described situation, is Liquid Relief Kit required or not?
A reference to a standard or code is preferred.
Thanks,
I have a DIB1 valve (10") that is used on a propane line; Propane's operating temperature is 150F and Operating pressure is 220 psia. At normal operating condition, propane is in vapor phase; However, in case of the valve closer, the temperature inside the valve cavity can fall below 110F (due to heat loss) and become liquid.
API 6D states:
"The manufacturer shall determine if the valve design could result in liquid being trapped in the body cavity in the open- and/or closed-valve position.
If liquid trapping is possible, the valve shall be provided with automatic cavity relief."
Now my question is that for described situation, is Liquid Relief Kit required or not?
A reference to a standard or code is preferred.
Thanks,