Dear Experts,

how to compare the pipe manifold nozzle with displacement for three operating temperature?. if it is a pump i should check as per API 610 but what about pipe manifold?


thanks & regards

baskar

Dear Baskar,
I would model the manifold as well to see the stresses on the manifold.

hi Aarif

thanks, but our battery limit is till manifold, in this case how can i solve? please give me your suggestion.



Thanks & Regards

Baskar

Dear Experts,

anybody can give me suggestion?

Baskar,
Can you please upload the drawing of the manifold? Then some of the experts may give you his opinion.

Dear Experts,

please find the attached model, what is the purpose of diplacement at the anchor of pipe manifold. is there any codes to check the pipe manifolds?


Thanks & Regards

Baskar

Even if this is B/L, it is a piece of piping. So you CAN model this system as well to suitable boundary conditions and analyze it. Any problem in that?

Hi Shahid,

Thank you, my question is how to resolve if we dont have an option to model together? because it is an existing plant and we are doing tie up to the exisitng pipelines.

Something to read:

http://65.57.255.42/ubbthreads/ubbthreads.php?ubb=showflat&Number=5303


http://www.betamachinery.com/uploadedFil..._Edge_Loads.pdf

contact the site or refer the old stress sketch for the boundary conditions.

At present all clients having old data base like : PDMS model and stress markup the with support functions and loads clearly marked on the stress iso.