SprinklerDesigner2
Mechanical
- Nov 30, 2006
- 1,251
Not in Florida I'm bidding a school where the fire department reports the results of their flow test as 55 psi static, 10 psi residual @ 540 gpm.
All sorts of things wrong with this (an 8 psi pitot?) and the only way I am going to bid it is with a stored water supply and fire pump for inside sprinkler only with the outside hydrants off the public system for outside hose stream.
I am thinking a 200 gpm @ 100 psi pump will do nicely.
The most demanding area I have is the kitchen. Actually laying out heads I need 177 gpm @ 25 psi at the pump suction flange. The kitchen is right next to the pump room.
I know not everyone does it this way but I've always sized the tank to supply 150% of the pumps rated capacity for the minimum time allowed. In this case using a 200 gpm pump in an Ord. Haz. Group II Occupancy I would call for 200*1.5*60=18,000 gallons.
In the past whenever it was up to me to size the pump I always did it this way.
The reality is all I need is 177*60=10,620 gallons.
But doing a demand calc, opening the same 9 sprinklers produces 308.2 gpm @ 63 psi or a 34 minute supply.
But it gets worse.
On a new system the C-Value of new black steel is 130 and at 150% the pump is really turning out 75 psi at not 65 psi. Given these realities the actual discharge would be 332 gpm or but a 32 minute supply for an Ordinary Hazard Occupancy.
But then, as I move the group of open heads closer to the cross main, it gets worse yet with a demand calc indicating less than a 30 minute (about 29 minutes) supply for this Ordinary Hazard Occupancy. Looking at the pump curve a 200 gpm pump will put out close to 400 gpm before it runs out of steam. Can't use it of course but just because I can't use 180% in my calculations doesn't mean it won't.
I always liked my old way of doing it but competition is to intense to be able to afford to give the customer more for his money.
Thoughts anyone?
All sorts of things wrong with this (an 8 psi pitot?) and the only way I am going to bid it is with a stored water supply and fire pump for inside sprinkler only with the outside hydrants off the public system for outside hose stream.
I am thinking a 200 gpm @ 100 psi pump will do nicely.
The most demanding area I have is the kitchen. Actually laying out heads I need 177 gpm @ 25 psi at the pump suction flange. The kitchen is right next to the pump room.
I know not everyone does it this way but I've always sized the tank to supply 150% of the pumps rated capacity for the minimum time allowed. In this case using a 200 gpm pump in an Ord. Haz. Group II Occupancy I would call for 200*1.5*60=18,000 gallons.
In the past whenever it was up to me to size the pump I always did it this way.
The reality is all I need is 177*60=10,620 gallons.
But doing a demand calc, opening the same 9 sprinklers produces 308.2 gpm @ 63 psi or a 34 minute supply.
But it gets worse.
On a new system the C-Value of new black steel is 130 and at 150% the pump is really turning out 75 psi at not 65 psi. Given these realities the actual discharge would be 332 gpm or but a 32 minute supply for an Ordinary Hazard Occupancy.
But then, as I move the group of open heads closer to the cross main, it gets worse yet with a demand calc indicating less than a 30 minute (about 29 minutes) supply for this Ordinary Hazard Occupancy. Looking at the pump curve a 200 gpm pump will put out close to 400 gpm before it runs out of steam. Can't use it of course but just because I can't use 180% in my calculations doesn't mean it won't.
I always liked my old way of doing it but competition is to intense to be able to afford to give the customer more for his money.
Thoughts anyone?