Dear all,
our piping system for liquefied gas is protected against line block with a small safety valve. It is boiling liquid at -160 deg. C, so not 'just' a thermal relief valve, however the required capacity is very low. Pipe design pressure is 16 bar.
The valves relief into a header, connected back to the tank gas phase, which is operating at 1 bar, but may be at 4 bar, which is its design pressure. So the backpressure is a variable superimposed back pressure, although the main source of backpressure changes very slowly with time and could be seen as a constant backpressure of maximum 4 bar.
I was planning on installing conventional safety valves set at 12 bar cdtp. Even with the tank at 4 bar, the valves would still open at 16 bar. The backpressure would influence the valve's capacity but if the remaining capacity is sufficient, the piping would be sufficiently protected. Blowdown is not an important parameter.
First question: is this allowed?
The contractor has decided to use balanced safety valves because his vendor has simply informed him that when backpressure is above 10% you need to use balanced type valves. But the valves are still set at 12 bar. I believe that if the tank is at 4 bar, the balanced safety valve will still open at 12 bar and not at 16 bar, which is also safe, but a waste of money.
Question 2: am I correct?
Thank you,
Edwin