nicknikolov
Mechanical
- Aug 7, 2020
- 3
I'll be inspecting and determining the integrity of a very old (installed 1965) surge tank used in a hydroelectric project.
The latest drawings on the project are all dated to 1965, and the tank is stated to have a corrosion allowance of 3/32".
Since this tank is not under pressure, I believe this corrosion allowance was arbitrarily picked. Also, since it is an old tank there will definitely be significant corrosion. Not sure if I should just stick to what was picked by the engineer that originally stamped the drawings, or if I should make a more specialized recommendation.
Are there any detailed reports or studies that have dealt with these non-code, non-pressurized tanks? If I see a single point with corrosion greater than 3/32" is that enough to condemn the tank, or at least require a new coating in the area?
The latest drawings on the project are all dated to 1965, and the tank is stated to have a corrosion allowance of 3/32".
Since this tank is not under pressure, I believe this corrosion allowance was arbitrarily picked. Also, since it is an old tank there will definitely be significant corrosion. Not sure if I should just stick to what was picked by the engineer that originally stamped the drawings, or if I should make a more specialized recommendation.
Are there any detailed reports or studies that have dealt with these non-code, non-pressurized tanks? If I see a single point with corrosion greater than 3/32" is that enough to condemn the tank, or at least require a new coating in the area?