Jun 27, 2020 #1 Hasab Chemical Joined Oct 7, 2019 Messages 28 Location SA Hi everyone, I want to know if there a case where the design pressure & design temperature of a branched line from an old line can be higher than the ones for that old line? (my opinion no such case exists). Thanks for the information.
Hi everyone, I want to know if there a case where the design pressure & design temperature of a branched line from an old line can be higher than the ones for that old line? (my opinion no such case exists). Thanks for the information.
Jun 27, 2020 #2 mk3223 Mechanical Joined Feb 4, 2006 Messages 1,488 Location US No doubt about it. Upvote 0 Downvote
Jun 27, 2020 #3 LittleInch Petroleum Joined Mar 27, 2013 Messages 23,004 Location GB Design yes, operating, no. But it wouldn't male much economic sense. Some numbers would help. Remember - More details = better answers Also: If you get a response it's polite to respond to it. Upvote 0 Downvote
Design yes, operating, no. But it wouldn't male much economic sense. Some numbers would help. Remember - More details = better answers Also: If you get a response it's polite to respond to it.
Jun 28, 2020 Thread starter #4 Hasab Chemical Joined Oct 7, 2019 Messages 28 Location SA Thanks bro mk3223 (Mechanical) & LittleInch (Petroleum), same as I guessed. Upvote 0 Downvote