rmarsenault
Civil/Environmental
- Jan 28, 2010
- 2
Hi folks.
I'm new here (posting that is). I have browsed this forum several times over the last few years. You guys are knowledgeable and it is nice to see such dedicated individuals in our field.
That being said, I am an engineer in Canada and my company is involved in fire protection engineering.
On a recent project, I designed the sprinkler, standpipe and fire pump system for a new 8 story office tower.
The AHJ (for lack of understanding) wanted NFPA 14 standpipe code followed to the letter. Therefore the standpipe system was required to be automatic and hence as you know have 100 psi available the remote hose connection. To achieve this a fire pump was required.
The static pressure was 45 psi and the pump rated at 110psi @ 750 gpm had a churn (no flow) pressure of 125 psi.
I specified a flat pump curve as I knew I had to have the maximum noflow pressure below 175psi as required by both NFPA 20 and NFPA 13(we didn't want to use high pressure fittings etc.).
So my no flow pressure was 45 psi + 125 psi, = 170 psi, below 175 psi.
Just the other day at the commissioning, in presence of the owner and contractor, during the pump test it was observed that the pump no flow pressure was 133 psi. Not 125 as specified. Doing the math, the max pressure is actually 178 psi. Now the owner and the prime consultant engineers are concerned that this exceeds what is required by code.
The parties involved are looking to me for advice and are wondering if pressure regulating devices should be installed.
Anyway I am wondering if any of you have had this case before and what do you think?
Personally I have noted pumps during testing always seem to give a little more than their design specs, but in this case I made it clear to the pump manufacturer that it was critical that the pump have the flat curve due to running so close to the max pressure condition...
regards
Rick M. Arsenault P.Eng
R M Arsenault Engineering Inc.
P.E.I., Canada
I'm new here (posting that is). I have browsed this forum several times over the last few years. You guys are knowledgeable and it is nice to see such dedicated individuals in our field.
That being said, I am an engineer in Canada and my company is involved in fire protection engineering.
On a recent project, I designed the sprinkler, standpipe and fire pump system for a new 8 story office tower.
The AHJ (for lack of understanding) wanted NFPA 14 standpipe code followed to the letter. Therefore the standpipe system was required to be automatic and hence as you know have 100 psi available the remote hose connection. To achieve this a fire pump was required.
The static pressure was 45 psi and the pump rated at 110psi @ 750 gpm had a churn (no flow) pressure of 125 psi.
I specified a flat pump curve as I knew I had to have the maximum noflow pressure below 175psi as required by both NFPA 20 and NFPA 13(we didn't want to use high pressure fittings etc.).
So my no flow pressure was 45 psi + 125 psi, = 170 psi, below 175 psi.
Just the other day at the commissioning, in presence of the owner and contractor, during the pump test it was observed that the pump no flow pressure was 133 psi. Not 125 as specified. Doing the math, the max pressure is actually 178 psi. Now the owner and the prime consultant engineers are concerned that this exceeds what is required by code.
The parties involved are looking to me for advice and are wondering if pressure regulating devices should be installed.
Anyway I am wondering if any of you have had this case before and what do you think?
Personally I have noted pumps during testing always seem to give a little more than their design specs, but in this case I made it clear to the pump manufacturer that it was critical that the pump have the flat curve due to running so close to the max pressure condition...
regards
Rick M. Arsenault P.Eng
R M Arsenault Engineering Inc.
P.E.I., Canada