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Design pressure & design temperature for a branched line

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Hasab

Chemical
Oct 7, 2019
28
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.
 
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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.
 
Thanks bro mk3223 (Mechanical) & LittleInch (Petroleum), same as I guessed.
 
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