Fidens
Mechanical
- Dec 9, 2013
- 6
Hi all,
I'm working on the stress analysis of a pipe rack, per B31.4. My question is based around the code requirements for expansion stress and correctly reflecting that requirement in the stress analysis load cases. From reading B31.4, section 402.5.2 (unrestrained pipe) it shows the equation for calculating the stress range resulting from thermal expansion and a note: "thermal stress should be calculated for the range of minimum and maximum operation temperatures"
If my T1 is my max and T2 is my min then:
1. Is it reasonable to assume that ambient temperature is my pipe metal temperature? Meaning, in the winter the average low is 10F and summer average high is 90F. As a result, my worst case scenarios are these temperatures(T1, T2) for my stress model. I'm aware that this approach neglects the fluid's heat transfer to the pipe during winter and vice-versa during summer (gasoline, expected to be around 68F) hence why I'm asking/confirming. Is that correct? If yes, then...
2. After creating my OPE cases (L1: W+T1+P1 & L2: W+T2+P1) I can segregate my full expansion stress range by doing L1-L2. This is saying that I'm taking the stresses calculated at min temp and adding them to the stresses calculated at max temp and getting this total "stress range". Is this understanding correct? If yes, then it complies with code requirements and the load case is correct. Yes? No?
Thank you in advance.
I'm working on the stress analysis of a pipe rack, per B31.4. My question is based around the code requirements for expansion stress and correctly reflecting that requirement in the stress analysis load cases. From reading B31.4, section 402.5.2 (unrestrained pipe) it shows the equation for calculating the stress range resulting from thermal expansion and a note: "thermal stress should be calculated for the range of minimum and maximum operation temperatures"
If my T1 is my max and T2 is my min then:
1. Is it reasonable to assume that ambient temperature is my pipe metal temperature? Meaning, in the winter the average low is 10F and summer average high is 90F. As a result, my worst case scenarios are these temperatures(T1, T2) for my stress model. I'm aware that this approach neglects the fluid's heat transfer to the pipe during winter and vice-versa during summer (gasoline, expected to be around 68F) hence why I'm asking/confirming. Is that correct? If yes, then...
2. After creating my OPE cases (L1: W+T1+P1 & L2: W+T2+P1) I can segregate my full expansion stress range by doing L1-L2. This is saying that I'm taking the stresses calculated at min temp and adding them to the stresses calculated at max temp and getting this total "stress range". Is this understanding correct? If yes, then it complies with code requirements and the load case is correct. Yes? No?
Thank you in advance.