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  1. look4advice

    Maximum operating Pressure (MOP) for a pipeline as per ASME B31.8

    Dear all, the point is: one pipeline is to be designed according to B31.8 and is protected by an upstream PSV. Knowing that usually the PSV overpressure is 10 % of the set pressure, how can I correctly define the design pressure of the pipeline, i.e. should I use as design pressure the PSV set...

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