I have an exchanger where HP gas is cooled against LP cooling water. The LP side (and local pipework up until the block valves) has had its design pressure increased according to the 10/13 rule, therefore there is no need for a local relief valve in the event of a tube rupture.
However, in such...
I have an exchanger where HP gas is cooled against LP cooling water. The LP side (and local pipework up until the block valves) has had its design pressure increased according to the 10/13 rule, therefore there is no need for a local relief valve in the event of a tube rupture.
However, in such...