We are designing a cooling water system for a petrochemical plant. As part of the design of the cooling tower, vent lines were added in the risers or the cooling tower. Hydrocarbons detection have been provided in these vents. However I would like to know how to size these vents. In some go-bys, we found that the vent lines have the same size of the risers.
As additionally information, our cooling water system is a closed loop and some heat exchangers has hydrocarbons at high pressure in the tube side. Relief valves for tube rupture have been provided for this heat exchangers.
I would like to know some guidelines to design the size of the vent lines to be added in the return line.
Best Regards and thanks