Cidona
Mechanical
- Oct 21, 2007
- 147
This site was just recently recommended to me and I am very happy to see the level of experience and knowledge in the posts.
With that said, I’m hoping I can get some advice on the correct direction to take with a situation I’m dealing with on a project I have.
The building is a new construction, 3 story, commercial property. Approx 28,00sq ft/ floor. Originally the project did not have hose valves included in the scope of work. The pump (installed), fed from an above ground tank, was sized for the sprinkler hydraulic calc areas. We ended up with a 110psi @ 1500 gpm. (ESFRs drove the calc).
Now we are required to provide 1½” FHVs in accordance with NFPA 13 2007, Section 8.17.5. We have 4 – 1½” FHVs (in the ESFR areas), and we are also providing 1” stations which are desired in addition by the insurance company
The calculation procedure required is outlined in 12.8 and is not required to have the 65/100 psi pressures required by NFPA 14. The hose demand is only required to be to be added to the beginning at the most remote station with each increment added at the pressure required by the sprinkler system design at that point.
The static and residual pressure on the hose line is restricted to 100psi. So we were going to use a pressure reducing valve to bring our static pressure down. I have not worked with PRVs before. I was thinking of using a 2½” Potter Roemer 4036 in an in-line installation to supply all the hoses , but after reviewing the valve it seems once the pressure on the inlet side of the PRV drops below the outlet static setting that there is a large ‘friction loss/pressure drop’. With not having a required pressure (other than having the pressure at the point of connection to the sprinklers) in the calc, the pump provides limited pressure at the hose under a flow situation (i.e. well below the outlet static setting 100psi)). To reduce it further doesn’t seem to be in good fire protection practice. While the static is in breach of the 100psi requirement, once in a flow situation the pressure is going to be less than that and would seem to be a preferable situation than complying with the static and dealing with the drop in pressure when it would be being used.
The individual 1½” PRVs seem to have the same problem.
The Tyco PRV-1 (pilot operated) also has the same problem.
So, I was wondering if anyone has come across this type of situation before. Any suggestions on products or solutions would be greatly appreciated.
Also, just to sneak it in here while on the PRV topic, when would you use a pilot operated PRV instead of the simpler (presuming less expensive) ‘regulating spring as part of the valve’ type offer by Potter Roemer/Zurn?
Thank you for any input. Sorry it was so long.
With that said, I’m hoping I can get some advice on the correct direction to take with a situation I’m dealing with on a project I have.
The building is a new construction, 3 story, commercial property. Approx 28,00sq ft/ floor. Originally the project did not have hose valves included in the scope of work. The pump (installed), fed from an above ground tank, was sized for the sprinkler hydraulic calc areas. We ended up with a 110psi @ 1500 gpm. (ESFRs drove the calc).
Now we are required to provide 1½” FHVs in accordance with NFPA 13 2007, Section 8.17.5. We have 4 – 1½” FHVs (in the ESFR areas), and we are also providing 1” stations which are desired in addition by the insurance company
The calculation procedure required is outlined in 12.8 and is not required to have the 65/100 psi pressures required by NFPA 14. The hose demand is only required to be to be added to the beginning at the most remote station with each increment added at the pressure required by the sprinkler system design at that point.
The static and residual pressure on the hose line is restricted to 100psi. So we were going to use a pressure reducing valve to bring our static pressure down. I have not worked with PRVs before. I was thinking of using a 2½” Potter Roemer 4036 in an in-line installation to supply all the hoses , but after reviewing the valve it seems once the pressure on the inlet side of the PRV drops below the outlet static setting that there is a large ‘friction loss/pressure drop’. With not having a required pressure (other than having the pressure at the point of connection to the sprinklers) in the calc, the pump provides limited pressure at the hose under a flow situation (i.e. well below the outlet static setting 100psi)). To reduce it further doesn’t seem to be in good fire protection practice. While the static is in breach of the 100psi requirement, once in a flow situation the pressure is going to be less than that and would seem to be a preferable situation than complying with the static and dealing with the drop in pressure when it would be being used.
The individual 1½” PRVs seem to have the same problem.
The Tyco PRV-1 (pilot operated) also has the same problem.
So, I was wondering if anyone has come across this type of situation before. Any suggestions on products or solutions would be greatly appreciated.
Also, just to sneak it in here while on the PRV topic, when would you use a pilot operated PRV instead of the simpler (presuming less expensive) ‘regulating spring as part of the valve’ type offer by Potter Roemer/Zurn?
Thank you for any input. Sorry it was so long.