thermmech
Mechanical
- Dec 13, 2004
- 103
As per UG-99, hydrostatic pressure is = 1.3 x MAWP X (Sall @ Tamb / Sall @ DT).
I have been presented an argument that the presence of vents and drains c/w blind flanges on SS vessels limits the hydrotest stress ratio, "Sall @ Tamb / Sall @ DT" to "1.0".
The vendor is stating that the bolting on the vents and drains (NPS 2 - 300# RFLWN) on the 316L SS vessel is the component that has the lowest hydrotest stress ratio.
I don't buy this argument as bolting has not been checked for the DP or MAWP and is a part of a standard assembly, which design is per ADME B16.5. Also, it is stated there that the hydro for piping components should be at 1.5x MAWP. Therefore, I believe that this bolting SHOULD NOT be taken into the account for determining lowest hydrotest stress ratio.
However, I believe if this was a S&T heat exchanger with a girth flange, that girth flange bolting could limit the ratio to 1.0.
Your comments would be appreciated.
I have been presented an argument that the presence of vents and drains c/w blind flanges on SS vessels limits the hydrotest stress ratio, "Sall @ Tamb / Sall @ DT" to "1.0".
The vendor is stating that the bolting on the vents and drains (NPS 2 - 300# RFLWN) on the 316L SS vessel is the component that has the lowest hydrotest stress ratio.
I don't buy this argument as bolting has not been checked for the DP or MAWP and is a part of a standard assembly, which design is per ADME B16.5. Also, it is stated there that the hydro for piping components should be at 1.5x MAWP. Therefore, I believe that this bolting SHOULD NOT be taken into the account for determining lowest hydrotest stress ratio.
However, I believe if this was a S&T heat exchanger with a girth flange, that girth flange bolting could limit the ratio to 1.0.
Your comments would be appreciated.