hull6851
Mechanical
- Dec 31, 2015
- 10
Let me preface this by saying that I am fairly uninformed in this industry as I previously was an engineer in a different industry. I have not had much luck in finding industry standard approaches on some of these issues, and my company doesn't have very good internal documents/standards, so I am hoping for some help here.
I am curious what the Oil and Gas industry experience and preference is for which types of valves shall be used with different types of process instrumentation specifically with pressure instrumentation (used on gas processing plants).
My understanding is that Pressure Gauges (Pressure Indicators) with Bourdon tubes should have a needle valve under the gauge since a ball valve, when opened suddenly, can cause damage to the Bourdon tube inside the gauge. That said, I am told that if an operator knows that they are doing, a ball valve could be opened slowly to avoid damage to the gauge, which still being preferable with regards to ease of operation when compared to needle valve (due to the time taken to operate the valve from one state to another).
Not knowing much about the instrumentation itself, can/should the above all apply also to Pressure Transmitters, Pressure Indicating Transmitters, Differential Pressure Indicators, and Differential Pressure Indicating Transmitters? How and why would the valves you would choose to use with the instrumentation differ?
I realize the answer might change for different service pressures and temperatures, but let's keep it simple and deal with only 150 pressure class and normal service temps (-20F to 250F).
If you need more information to form a quality response, please kindly ask for it, taking into consideration my ignorance and desire to learn! I am happy to entertain intelligent discussion to be better informed.
Thanks!
I am curious what the Oil and Gas industry experience and preference is for which types of valves shall be used with different types of process instrumentation specifically with pressure instrumentation (used on gas processing plants).
My understanding is that Pressure Gauges (Pressure Indicators) with Bourdon tubes should have a needle valve under the gauge since a ball valve, when opened suddenly, can cause damage to the Bourdon tube inside the gauge. That said, I am told that if an operator knows that they are doing, a ball valve could be opened slowly to avoid damage to the gauge, which still being preferable with regards to ease of operation when compared to needle valve (due to the time taken to operate the valve from one state to another).
Not knowing much about the instrumentation itself, can/should the above all apply also to Pressure Transmitters, Pressure Indicating Transmitters, Differential Pressure Indicators, and Differential Pressure Indicating Transmitters? How and why would the valves you would choose to use with the instrumentation differ?
I realize the answer might change for different service pressures and temperatures, but let's keep it simple and deal with only 150 pressure class and normal service temps (-20F to 250F).
If you need more information to form a quality response, please kindly ask for it, taking into consideration my ignorance and desire to learn! I am happy to entertain intelligent discussion to be better informed.
Thanks!