yeah, that guy. I've tried to call him but.... And he never replies to RFIs.

On Tue, Mar 22, 2016 at 10:05 AM, Bill Brooks <[email protected]>
wrote:

> And sometimes the hose used to connect the pumper to the FDC is an issue as
> well if it is not rated for higher pressures.
>
> I know this is something we toss back a forth but shouldn't the Engineer of
> Record be the person to do this legwork ahead of time?
>
> Bill Brooks
> Brooks Fire Protection Engineering
>
> -----Original Message-----
> From: Sprinklerforum [mailto:
> [email protected]]
> On Behalf Of Steve Leyton
> Sent: Tuesday, March 22, 2016 12:34 PM
> To: [email protected]
> Subject: RE: Standpipe Calc: Adding City Demand to Pumper Truck?
>
> Attention Everybody (and Sean):
>
> It is time for us as an industry to move outside the box.   Prescriptive
> codes and standards are convenient, and most AHJ's will defer to them
> without amendment or interpretation because it's usually not required to do
> so.   But sometimes we have to address situations that ARE subjective and
> this is one of those - you have to meet with the serving fire department to
> verify their operational practices and pumping capabilities.  Your
> statement
> that the pumper is "... sized for 150psi at 1000gpm" isn't accurate;
> generally, modern pumpers and engines can make up to 300 PSI at either
> 1,000
> or 1,500 GPM so available pressure isn't the issue.  Design of the system
> and identification of the demand are the issues.    150 PSI is an industry
> practice, not an absolute threshold that can't be crossed and NFPA 14 has a
> requirement that you must hang a sign on the FDC informing the FD of the
> required pressure to meet the calculated demand.
>
> As with sprinkler systems, Pressure = $$, so the more you have the smaller
> the piping can generally be and you save $$.   150 is a safe starting
> pressure so most FD's will require that you use that as a source pressure;
> if a manual standpipe system is a little longer or taller and requires more
> pressure we can make that up by subbing 6" for 4" and it still works at
> 150.
> But in taller buildings, you will need more pressure so, if you want to do
> a
> 70' tall building  with 4" risers all the way up the shafts, then you have
> to obtain FD approval to pump at 195 or 215 or whatever it turns out to be.
> And, you have to build the system out of components rated for that
> pressure,
> which is actually no big deal these days.    And when it's over, you badge
> the FDC with a sign that states, "PUMP 1000 GPM AT 215 PSI TO MEET DEMAND
> AT
> STAIR #2 ROOF" or something like that (your FD will tell you how to word
> the
> sign).
>
> Partner up people ...
>
> The preceding is my opinion only and does not represent the opinion of or
> an
> interpretation of the standard by NFPA or the Technical Committee on
> Standpipes.
>
> Steve L.
>
> -----Original Message-----
> From: Sprinklerforum [mailto:
> [email protected]]
> On Behalf Of [email protected]
> Sent: Tuesday, March 22, 2016 8:31 AM
> To: [email protected]
> Subject: RE: Standpipe Calc: Adding City Demand to Pumper Truck?
>
> Sorry for coming into this a week late.  We have recently been dealing with
> specs and AHJ requirements that state we need to supply 130psi and/or
> 140psi
> at the top outlet regardless of whether it is manual or automatic.  Same
> flows as outlined in NFPA 14 (500gpm +250gpm per standpipe up to 1000gpm).
> The fire pumper truck is still sized for 150psi @ 1000gpm.  What do you
> suggest we do if we can only set the FDC to be the source of 151@0 and
> 150@1000?  Some building are still 70ft tall and the standpipe is still a
> manual wet.  Only accounting for elevation we are looking at 160psi/170psi
> demand at the FDC.  Even if your answer is make it an automatic standpipe,
> the 140psi requirement limits the "manual" standpipe building height to
> 23ft
> when we don't account for friction loss using your calculation procedure.
> So we can't even meet these manual FDC 150psi calcs on a building that
> doesn't even need a standpipe.
>
> Thanks,
> Sean VG
>
>
>
> -----Original Message-----
> From: Sprinklerforum [mailto:
> [email protected]]
> On Behalf Of Steve Leyton
> Sent: Monday, March 14, 2016 3:57 PM
> To: [email protected]
> Subject: RE: Standpipe Calc: Adding City Demand to Pumper Truck?
>
> Tony:
>
> You (or the submitter) are over-simplifying what the annex says.  It's not
> the intent that you take the city flow test and add it to the pumper curve.
> NFPA 1901 sets the basic performance curve for a pumper at 150 PSI/1,000
> GPM.   NFPA 13E is the standard for FD Operations for buildings equipped
> with sprinklers and standpipes - that standard goes into the company
> engineer's procedure for calculating the discharge pressure of the pump
> based on suction pressure, friction loss in hose and other variables.   But
> the bottom line is that it's all targeted at discharging 150 PSI residual
> at
> 1,000 GPM.   This has NOTHING to do with pressure at the FDC; it has to do
> with calculating the performance of the apparatus.   What gets to the FDC
> is
> up to the engineer.
>
> Which is why 7.7.4 states, "When the system demand to be supplied by the
> fire department at the fire department connection is being determined, the
> local fire department shall be consulted regarding the water supply
> available from a fire department pumper."    FROM A FIRE DEPARTMENT PUMPER.
> It's up to the incident commander and his or her engineer to determine the
> suction pressure and set their discharge to whatever is required to make
> their programmed starting pressure.  And based on the nationwide standard
> and best practices, that is almost certain to be 150 PSI at the prescribed
> flow rate.  The engineer will calculate the friction loss in the discharge
> hose that's connected to the building.  If you are reviewing plans that
> show
> 150 PSI residual plus a positive suction head at that flow rate as the
> inlet
> pressure, then that is almost certainly not correct.
>
> To answer your question, if I have a building with two (750 GPM) or three
> or
> more (1,000 GPM) standpipes, we plug in a "flow test" static pressure of
> 151
> PSI and a residual of 150 PSI at the target flow rate and we run the calc'
> using the FDC as the "city connection".    We plug in a 500 PSI hose stream
> allowance at the most remote standpipe outlets and at 250 GPM hose streams
> at those points in the bulk main system where the other risers take off.
> We
> allow 5 PSI for loss in a standard hose valve so the minimum pressure at
> any
> node is 105 PSI.
>
> The foregoing is my opinion only and does not represent the opinion of or
> any manner of interpretation by NFPA or the Technical Committee on
> Standpipes.
>
> Steve Leyton
>
> -----Original Message-----
> From: Sprinklerforum [mailto:
> [email protected]]
> On Behalf Of Tony Eggster
> Sent: Monday, March 14, 2016 3:24 PM
> To: [email protected]
> Subject: Standpipe Calc: Adding City Demand to Pumper Truck?
>
> Quick question: I'm reviewing some plans for a manual class I standpipe and
> the designer added the city flow test to the usual 1000gpm fire pumper
> curve
> in order to keep all the pipe down to 4". I see in the NFPA 14 appendix
> that
> you can do this but personally I've always just calculated solely to the
> pumper curve. How do you guys do it?
>
> Also, I'm assuming that if you do factor in city supply wouldn't that
> frequently require high pressure pipe and fittings depending on city supply
> psi?
>
> _TONY
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-- 
Ron Greenman
Instructor
Fire Protection Engineering Technology
Bates Technical College
1101 So. Yakima Ave.
Tacoma, WA 98405

[email protected]

http://www.bates.ctc.edu/fireprotection/

253.680.7346
253.576.9700 (cell)

Member:
ASEE, SFPE, ASCET, NFPA, AFSA, NFSA, AFAA, NIBS, WSAFM, WFC, WFSC

They are happy men whose natures sort with their vocations. -Francis Bacon,
essayist, philosopher, and statesman (1561-1626)

A problem well stated is a problem half solved. -Charles F. Kettering,
inventor and engineer (1876-1958)
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