DavidCR
Mechanical
- Jan 10, 2002
- 359
I have a hydro power plant fire protection system where the water is supplied by a gravity water tank.
The tank elevation is 133m (420´)above the PVC-C900 private service mains. So on static, and almost a plain curve on flow conditions, the pressure bellow will be aprox. 182psi. On the lower floors of the power house the static pressure gets to 214psi. There is no chance to relocate the tank.
AHJ here asks for pressure to be regulated to 65/85 psi for classII/classI hose stations. So I´m thinking of using hydraulic control type FM-UL type pressure reducing valves for flow conditions. Vendors (Claval,Watts,Bermad)of this valves recomend to use two parallel valves of different size in order to get a steady flow for a wide range of flows, one would work for low flows (i.e.a hose) and the other would work for the design full demmand scenario (as to NFPA 851).
Furthermore, AHJ here asks for a by-pass parallel line as an override of the pressure control devices, in order to guarantee the supply even it is not regulated for the case where the pressure reducing valves are in maintenance or if there is a failure. Here we had a fire in a alcohol plant where the pressure reducing valve failed and the water system was inoperative.
Inside the power house there is a sprinkler system and it is bellow ground level (479´bellow the tank) 208psi so class 175 sprinklers and devices will be in "danger".
My question...
I´m wondering that I will need also a main pressure relief valve (like the one required for a fire pump) to prevent overpressure on the accesories. And this will prevent overpressure when the bypass override is used, or when adjusting the pressure reducing valves, or if it fails t o adjust.
Initially I was thinking of small relief valves, but I suppose they work only for the case of closed systems that may suffer overpressure from cases like trapped air effects, day thermal cycles, etc. may develope overpressure. But in this case I suppose a small relief valve will not have the capacity to relief the pressure from the gravity tank.
Other option will be to go up in pressure class of devices. But I´m not sure if I will have money of availability problems.
I´d appreciate any comment on this case, if my thoughts about the main relief valves sounds fine, or if you could suggest any another idea on how to prevent presure problems, or if I´m mising something.
Thanks in advance.
The tank elevation is 133m (420´)above the PVC-C900 private service mains. So on static, and almost a plain curve on flow conditions, the pressure bellow will be aprox. 182psi. On the lower floors of the power house the static pressure gets to 214psi. There is no chance to relocate the tank.
AHJ here asks for pressure to be regulated to 65/85 psi for classII/classI hose stations. So I´m thinking of using hydraulic control type FM-UL type pressure reducing valves for flow conditions. Vendors (Claval,Watts,Bermad)of this valves recomend to use two parallel valves of different size in order to get a steady flow for a wide range of flows, one would work for low flows (i.e.a hose) and the other would work for the design full demmand scenario (as to NFPA 851).
Furthermore, AHJ here asks for a by-pass parallel line as an override of the pressure control devices, in order to guarantee the supply even it is not regulated for the case where the pressure reducing valves are in maintenance or if there is a failure. Here we had a fire in a alcohol plant where the pressure reducing valve failed and the water system was inoperative.
Inside the power house there is a sprinkler system and it is bellow ground level (479´bellow the tank) 208psi so class 175 sprinklers and devices will be in "danger".
My question...
I´m wondering that I will need also a main pressure relief valve (like the one required for a fire pump) to prevent overpressure on the accesories. And this will prevent overpressure when the bypass override is used, or when adjusting the pressure reducing valves, or if it fails t o adjust.
Initially I was thinking of small relief valves, but I suppose they work only for the case of closed systems that may suffer overpressure from cases like trapped air effects, day thermal cycles, etc. may develope overpressure. But in this case I suppose a small relief valve will not have the capacity to relief the pressure from the gravity tank.
Other option will be to go up in pressure class of devices. But I´m not sure if I will have money of availability problems.
I´d appreciate any comment on this case, if my thoughts about the main relief valves sounds fine, or if you could suggest any another idea on how to prevent presure problems, or if I´m mising something.
Thanks in advance.