jamesbanda
Chemical
- Sep 21, 2004
- 223
Dear sirs,
We have been reviewing our common relief stacks for a design of a plant. Can i ask if the relief stack is pointed a high elevation say 40 meters or ~120 feet and say 10-15 relief valves discharge into the commnon header..
is their merrit in nitrogen purging the header..
- dp calcs on rv's limit pressure rise to <1 barg (or lower)
- worse case pipework withstand an explosion 10x pressure rise..and probably unlikely carbon steel equipment and relief valve force would push air out..and it is every unlikely
- does n2 purges prevent atomspheric corrision ? probably not as carbon steel forms a corrision barrier after time
- prevent water ingress - maybe but we have drains anyhow.. and these are regually checked..
- so with no process vents into a common header why would you use a nitrogen purge..
We have been reviewing our common relief stacks for a design of a plant. Can i ask if the relief stack is pointed a high elevation say 40 meters or ~120 feet and say 10-15 relief valves discharge into the commnon header..
is their merrit in nitrogen purging the header..
- dp calcs on rv's limit pressure rise to <1 barg (or lower)
- worse case pipework withstand an explosion 10x pressure rise..and probably unlikely carbon steel equipment and relief valve force would push air out..and it is every unlikely
- does n2 purges prevent atomspheric corrision ? probably not as carbon steel forms a corrision barrier after time
- prevent water ingress - maybe but we have drains anyhow.. and these are regually checked..
- so with no process vents into a common header why would you use a nitrogen purge..