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1
- #1
ehbadger
Chemical
- Oct 7, 2015
- 119
Hi all, I've got three main questions I am curious about. All are more specific to 'non-metallic' gaskets (Examples being Sigma 533, GYLON 3510, GORE UPG) but I am open to other responses as well. Most of my experience is 150# to 300# service, raised face flanges, <350F temps.
1) Where you have the choice, which style do you prefer: RING or FULL-FACE?
--> We use both currently, but the FULL-FACE are definitely more 'foolproof' to install. I'm curious to what other plants have standardized on and why.
--> If you use RING style gaskets, why?
2) What dimensions do you use: 'OLD' ANSI (smaller ID) or 'NEW' ANSI (larger ID)?
--> See the differences here: --> We prefer 'OLD' style so an uncompressed portion of gasket can hang inside the pipe ID ever so slightly. Once the joint is torqued, that overhanging inner section "locks" the gasket and helps prevent blowout or radial creep. This is not achieved with the 'new' dimensions. The minor disruptions to fluid flow or contact with process is not a concern.
3) Do you have any training, tips, tricks, etc for installing RING gaskets correctly (centered between the flanges)?
--> The majority of gasketing issues I see are related to misaligned ring gaskets (read: not getting a complete inner ring overhanging in the pipe ID) cold-flowing and eventually pushing out radially until a leak path develops. See attached photo.
We have very good mechanics with torque tables, gasket selection, and all that. Gasket issues are very uncommon. But they do crop up. And I am curious as to what might be "best practice" or how other people handle ring gaskets.
Thanks!
ninja edit: added photo of ring gasket failure mechanism:
1) Where you have the choice, which style do you prefer: RING or FULL-FACE?
--> We use both currently, but the FULL-FACE are definitely more 'foolproof' to install. I'm curious to what other plants have standardized on and why.
--> If you use RING style gaskets, why?
2) What dimensions do you use: 'OLD' ANSI (smaller ID) or 'NEW' ANSI (larger ID)?
--> See the differences here: --> We prefer 'OLD' style so an uncompressed portion of gasket can hang inside the pipe ID ever so slightly. Once the joint is torqued, that overhanging inner section "locks" the gasket and helps prevent blowout or radial creep. This is not achieved with the 'new' dimensions. The minor disruptions to fluid flow or contact with process is not a concern.
3) Do you have any training, tips, tricks, etc for installing RING gaskets correctly (centered between the flanges)?
--> The majority of gasketing issues I see are related to misaligned ring gaskets (read: not getting a complete inner ring overhanging in the pipe ID) cold-flowing and eventually pushing out radially until a leak path develops. See attached photo.
We have very good mechanics with torque tables, gasket selection, and all that. Gasket issues are very uncommon. But they do crop up. And I am curious as to what might be "best practice" or how other people handle ring gaskets.
Thanks!
ninja edit: added photo of ring gasket failure mechanism: