SFuller
Chemical
- Jul 7, 2003
- 8
Dear All,
We are installing a 8" new steam line on site. The line is a branch from the site main header and will contain 7 barg saturated steam. The end points for the line are slightly off-set from each other so there are two 90º elbows in the line with a short section running between them.
When we had stress analysis done on the line the engineering consultant indicated that we needed to allow for some movement in the line due to expansion. They gave us two options:
1 Install a bellows in the short section that runs at 90º to the general direction of the line to allow for lateral movement of the bellows.
2 Install an expansion loop in the line by fitting a few more elbows and allowing some extra pipe.
Obviously, either solution should work if properly designed and installed.
As a process/chemical engineer I am inclined towords using the second option (an expansion loop) as any refernce book on industial disasters is full of references to bellows failing. My mechanical colleagues wish to install the bellows as it is a cheaper solution and will save them from having to re-design the line to accomodate the loop.
Do any of you have an opinion or good/bad experience of either solution that you could share with me?
Thanks,
Steve
We are installing a 8" new steam line on site. The line is a branch from the site main header and will contain 7 barg saturated steam. The end points for the line are slightly off-set from each other so there are two 90º elbows in the line with a short section running between them.
When we had stress analysis done on the line the engineering consultant indicated that we needed to allow for some movement in the line due to expansion. They gave us two options:
1 Install a bellows in the short section that runs at 90º to the general direction of the line to allow for lateral movement of the bellows.
2 Install an expansion loop in the line by fitting a few more elbows and allowing some extra pipe.
Obviously, either solution should work if properly designed and installed.
As a process/chemical engineer I am inclined towords using the second option (an expansion loop) as any refernce book on industial disasters is full of references to bellows failing. My mechanical colleagues wish to install the bellows as it is a cheaper solution and will save them from having to re-design the line to accomodate the loop.
Do any of you have an opinion or good/bad experience of either solution that you could share with me?
Thanks,
Steve