Can anyone please state your experience to derate MAOP of a corroded pipeline using ASME 31G? Is the result obtained by using B31G reliable? Any good or bad experience? What is the difference bwteen B31G, B31G modified, and RSTRNG method? Any advantage o using one method over the other one? How prevalent is it offshore pipeline system, specially Gulf of Mexico Area? Can anyone point me towards right direction to get more info. Thanks.
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