Hello,
I was recently involved as the junior engineer on a project that required us to rate an existing low pressure flare header for size over various plant overpressure scenarios. Each storage tank is connected to the Low Pressure flare line through a PVSV that will "pop" if the maximum allowable pressure in the tank is met. It was clear from the beginning that in the case of a fire the "current" low pressure flare header does not have the capacity to relieve the storage tank vapours. The end result is that we made sure that the the EPRV and the thief hatch on each tank was sized correctly for the fire case but, we didn't size the LP flare header for the fire case. So in the case of a fire the tank vents to atmosphere.
I am just curious to see if this is standard practise? It seems obvious (but with my limited experience I could be wrong) that most LP Flare headers would not be able to handle tank vapour due to fire (unless they have a very large header). Anyway, I will appreciate any discussion I could have about this with anyone......I am just trying to increase my knowledge base.
Thanks!
Edited by KeJoSa2010, 08 August 2013 - 10:28 AM.