Re: Stress Analysi on Design temp or Operating temperature

From: <HPRAJAPATI@ltcis.ltindia.com>
Date: Wed May 31 2006 - 00:16:00 EDT

Stress analysis shall be done for design / operating / regneration / any other special case defined in P&ID or process. Stress & Nozzles should be safe in all possible cases of operation same way restraints shall be designed to withstand maximum possible piping loads in all possible operating cases. Analysist should envisaged all possible temperature cases for piping stress analysis.

Regards,

"Mohammad Danish" <mdanish@tebodin.co.om> Sent by: <a href="/group/PipingDesign/post?postID=_98sF6tsx4-MoqurKdC0dQFME9nQbLhwm5DVLLfNOIuYMdIL0rF_2roiebxmNXTOB4-n-Nl7CYJ8ShlW4bhnwjW5JeFJ3PE">PipingDesign@yahoogroups.com</a> 29/05/2006 02:14 PM
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<lbrown@coade.com>
Subject
[PipingDesign] Stress Analysi on Design temp or Operating temperature

Dear Friends,

Please advice me for doing stress analysis we should use design

temperature or Maximum operating Temperature?

If we refer CAESER II, Then the help says that among the 9 Temperature

fields the maximum operating temperature to be used.( Maximum operating

temp appears to be the maximum)

Please advice.

Regards,

Tebodin & Partner LLC

Md Danish

Jr Pipeline Engineer

tel. +968-2449 6077

fax +968 2449 7290

gsm +968 95525965

e-mail <a href="/group/PipingDesign/post?postID=4acwL0uXo-NqHYZm8hsNon8sdHykIQmgz4pbX8liDfIGuyflXGAPFYl0i213vp6SlBbl7a-ZNaBGzV7Q">mdanish@tebodin.co.om</a>

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[Non-text portions of this message have been removed] Received on Wed May 31 00:16:00 2006