StressGuy
Mechanical
- Apr 4, 2002
- 484
I'm struggling to find some references on how to approach this particular problem - at what point does a pipe need to be on a shoe/saddle support due to the local stresses at the support location?
For larger lines, I'm used to them being on a saddle for insulation and/or because they need to be sloped for draining. From that, I've used variations of the Zick analysis and various saddle design tools to check the horn stresses and such. That's all well charted territory.
In this case, I've got a vapor line, uninsulated, and unsloped. So, all the normal triggers that would put this line on shoes aren't in play.
So now I'm having to approach this from a pure structural integrity standpoint. It's intuitively obvious that there is some threshold where a liquid filled pipe is going to need the reinforcement of a support saddle to keep it from ovalizing. Every horizontal pressure vessel already does it. Finding a mathematical basis to determine that threshold is proving difficult.
Does anyone have any reference papers that address this topic? I'll happily run calcs or built a spreadsheet to do an evaluation. Even some kind of general guideline, like a D/t ratio that has some industry agreement would help.
Edward L. Klein
Pipe Stress Engineer
Houston, Texas
"All the world is a Spring"
All opinions expressed here are my own and not my company's.
For larger lines, I'm used to them being on a saddle for insulation and/or because they need to be sloped for draining. From that, I've used variations of the Zick analysis and various saddle design tools to check the horn stresses and such. That's all well charted territory.
In this case, I've got a vapor line, uninsulated, and unsloped. So, all the normal triggers that would put this line on shoes aren't in play.
So now I'm having to approach this from a pure structural integrity standpoint. It's intuitively obvious that there is some threshold where a liquid filled pipe is going to need the reinforcement of a support saddle to keep it from ovalizing. Every horizontal pressure vessel already does it. Finding a mathematical basis to determine that threshold is proving difficult.
Does anyone have any reference papers that address this topic? I'll happily run calcs or built a spreadsheet to do an evaluation. Even some kind of general guideline, like a D/t ratio that has some industry agreement would help.
Edward L. Klein
Pipe Stress Engineer
Houston, Texas
"All the world is a Spring"
All opinions expressed here are my own and not my company's.