I am calculating a vent valve for an atm storage tank (V=2000 m3)
The tank is used to store water solution at around 90 C. (solution boiling point = 120C) Steam coil is equipped (3.5barg saturate steam)
API2000 doesn't elaborate the steam tube rupture case. Some adviced to use API520 HX tube rupture case. But I don't think it is a comparable case as tank has quite larger bulk liquid.
In my opinion, it makes more sense to take the coil rupture case as a steam inject heater. The leaking steam is actually condensed in the liquid.
Venting capacity should be the volume of condensed steam and condensate from heating coil.
It would be great if someone in this forum could confirm if the steps i am taking are correct or if there is something i should take into account.
Thank in advance,