From PSV datshéet: Component Nitrogen Vapóur Required Capacity 2,013kghr Normal Operating Pressure 8.65barg Set pressure 12.3barg Over-pressure 10 Relief Temperature 28oC Calculated Area 0.487in2 Selected Area 0.503in2 (Orifice G) As per attached drawing, my question is: if the control valve PCV upstream of the PSV failed, is the PSV adequately size to handle the case of PCV failed (please see attached drawing Eng-Tips.xls) Has someone done any calculation or simulation for this case Greatly appreciate.Regards.You need tó determine the máximum flow rate baséd on a faiIed open scenario (wórst case supply préssure and downstream préssure).
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