GD2, Thank you for your response,
I am aware of the complexity of this work. I have just to prepare preliminary plans. I try to learn more about the subject.
Thanks for your precious advices!
Thank you jari001 for your response.
My maximum operating pressure is 8 bar, according to NORSOK standard, my maximun operating pressure is about 11,5 bar. When the discharge is blocked; or in fire case, pressure will rise above DP.
Hello,
As part of the development of a PID, I am looking to install pressure relief valves (PRV).
My system operates under pressure (8bar).
Do I have to provide PRV on each line and each equipment of the installation?
Am I obligated,in accordance with norms, to set up PRVs on each equipment...
Thanks you littleinch for your response.
I forgot that posting to multiple forums is prohibited, so I deleted the other one.
Exuse me but you have an offensive answering manner.
In response to your questions:
SRV is a typo, I talk about PRV all the time. I haven't steam in my installation.
The...
Thank you Latexman for your response.
Yes you are right I am freshly graduated and this is the first time that I have to developed PID.
Unfortunately I cannot find the answer to my question in my entourage, and I do not know much about standards, I wanted just to know if there is a norm that...
Hello,
As part of the development of a PID, I am looking to install pressure relief valves (PRV).
My system operates under pressure.
Do I have to provide PRV on each line and each equipment of the installation?
Am I obligated,to cofrom norms, to set up PRVs on each equipment under pressure?
The...
Hello,
I need to choose the right pipe diameter knowing the flowrate. is there a minimum gas velocity and a maximum gas velocity standardized to be respected?
Thank you
Hello,
I need to know how to estimate an inert gas (N2) flowrate used for O2 remove from reactor and pipelines. (PS The O2 concetration is unknown)
Thank you
Thank you for your response.
In fact I can't close the valve, I need this flow continuously, I just want to have a constant pressure inside the vessel.
Hello,
I want to know if it is possible to regulate the pressure inside an equipement by an upstream valve controlled by a pressure controller?
i.e. if the pressure drops the pressure transmitter sends a cosign to the controller which open the valve?
Thank you
Hello,
I want to switch a gas flow from line A to line B.
This gas is injected into my reactor at a point A (flow Q and a pressure P).
For maintenance reasons, a part of this reactor which contain injector A is isolated and the gas switches to the line B.
The second injector B supplies the...
