traineeprocessengg
Chemical
- Mar 20, 2019
- 1
In my current project, there is a vessel which was receiving low pressure steam condensate and medium pressure steam condensate. In front of the nozzles for those, there was a flipped L shaped attachment. When I looked into the vessel datasheet it said that it was an internal baffle.
Is it there to somewhat reduce the effect of two phase flow which might occur if the steam (which is being sent to heat exchangers) doesn't condense fully? The vessel is small with a 1 m diameter and 3.5 m T/L to T/L length. I am assuming that it is protection against water hitting the vessel wall at high velocity if steam doesn't condense fully. Is that assumption correct?
Has anyone come across this?
Is it there to somewhat reduce the effect of two phase flow which might occur if the steam (which is being sent to heat exchangers) doesn't condense fully? The vessel is small with a 1 m diameter and 3.5 m T/L to T/L length. I am assuming that it is protection against water hitting the vessel wall at high velocity if steam doesn't condense fully. Is that assumption correct?
Has anyone come across this?