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  1. adx

    About vessel design temperature

    Hi! There is a problem I am suffering with in fire exposure scenario: A PSV to service product cut tank, the bubble point of bulk liquid @ MAWP is far higher than MAWT, how should I do ? More details, the MAWT of product cut tank is 205C, but the PSV/RD action temperature @ MAWP (1barg) is...

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