MGXFP
Mechanical
- Jul 30, 2002
- 411
Hello all.
I've very little experience with standpipes and NFPA14 and would like some help.
The subject is a Class I standpipe. The requirement for calculations are two 2 1/2" hose valves flowing 250 GPM each at a pressure of 100 PSI along with, of course, the top hose valve on all other standpipes flowing the same.
In my calculations I'm not certain whether or not to derive a K factor of 25 for the valve and flow it like a fire sprinkler on the standpipe or to model a short 2 1/2" length of pipe with a friction loss for a mechanical tee.
The difference in pressure isn't great between both methods so I have no concern of not meeting the safety factor but I would like some input from more experienced designers and engineers as to what would be most correct.
Thanks!
I've very little experience with standpipes and NFPA14 and would like some help.
The subject is a Class I standpipe. The requirement for calculations are two 2 1/2" hose valves flowing 250 GPM each at a pressure of 100 PSI along with, of course, the top hose valve on all other standpipes flowing the same.
In my calculations I'm not certain whether or not to derive a K factor of 25 for the valve and flow it like a fire sprinkler on the standpipe or to model a short 2 1/2" length of pipe with a friction loss for a mechanical tee.
The difference in pressure isn't great between both methods so I have no concern of not meeting the safety factor but I would like some input from more experienced designers and engineers as to what would be most correct.
Thanks!