Hi all,
I'm just trying to size a PSV downstream of a low pressure gas regulator. I don't have a Cv or orifice size, only a nominal flow and flow curves. Can these be used to determine failure flowrates?
The regulator in question is fed at 4 barg and will be relieved by the PSV at .1 barg.
See the attached pdf for the data I have on the regulator.
Any help is much appreciated. Cheers.