What editions of #20 and #25 are referenced and following?

> On 03/06/2026 11:24 AM EST Fpdcdesign <[email protected]> wrote:
>  
>  
>  
> Brett, here is Todd’s take (having seen a lot of pumps with issues lately):
>  
> 1. Make sure you have the 10X pipe diameter distance between the backflow 
> preventer and the pump suction. 
>  
> 2. Based on the pump test, you have a 750 gpm pump rated at 70 psi and 
> producing only 65 psi at 750 gpm during the test. 63 psi would be a failed 
> test. How does that compare with previous tests? It could be an issue with 
> the pump or the suction piping. It is a 51 year old pump. Needs 
> investigating. 
>  
> 3. You need to get a hydrant flow test. I wouldn’t touch a pump project 
> without one. 
>  
> 4. You need to do a standpipe calculation to see what your demand is at the 
> pump discharge. 
>  
> 5. Don’t draw the public supply below 20 psi during a test.
>  
> 6. There is a section in NFPA 25 that states that if a pump cannot be tested 
> to 150%, but it can be tested to the greater of system demand or rated flow, 
> then it can be considered acceptable. 
> 
> Todd G Williams, PE
> Fire Protection Design/Consulting
> Stonington, CT
> 860-535-2080 tel:860-535-2080 (ofc)
> 860-554-7054 tel:860-554-7054  (fax)
> 860-608-4559 tel:860-608-4559 (cell)
> 
> 
> 
> > On Mar 6, 2026 at 10:52 AM, <Chris Dorn 
> > mailto:[email protected]> wrote:
> > 
> > 
> > Questions
> > 
> > 1. If testing confirms the standpipe cannot achieve 65 psi at 750 GPM, what 
> > is the recommended course of action?
> > Install a higher pressure fire pump. 150% is not a requirement. 65psi 
> > definitely is though. Fire pumps make pressure, not water.
> > 
> > 2. How should we address the requirement for a backflow preventer when pump 
> > suction is already low at 150% flow?
> > 
> > Again not a requirement.
> > 
> > 1. Are there alternative design approaches to meet the water authority’s 
> > requirement while maintaining proper pump operation?
> > 
> > The water purveyor is protecting their system from a backflow situation. 
> > They are not going to let this go.
> > 
> > 1. Water authority wants the backflow detector assembly on the suction side 
> > of the pump.
> > 
> > Find the lowest pressure loss backflow device and go with it.
> > 
> > Just my opinion.
> > 
> > Chris
> > 
> >  
> > 
> >  
> > 
> >  
> > 
> > From: Brett Barrall <[email protected]>
> > Sent: Friday, March 6, 2026 9:55 AM
> > To: [email protected]
> > Subject: [Sprinklerforum] Backflow Preventer on Fire Pump Suction
> > 
> >  
> > 
> > Hello!
> > 
> >  
> > 
> > This is my first time posting, I’ll try to keep it short.
> > 
> >  
> > 
> > We have a project with a new customer where the water authority is 
> > requiring a backflow preventer on the suction side of an existing fire 
> > pump. We want to confirm the proper approach due to potential hydraulic 
> > concerns.
> > 
> > * Building height: 130 ft
> > 
> > * System type:  Wet pipe sprinkler and standpipe
> > o Stair Tower 1: Class III combined automatic standpipe
> > 
> > o Stair Tower 2: Automatic Class III standpipe
> > 
> > o Standpipe flow requirements – 65 psi at 750 gpm (System installed 1975)
> > 
> >  
> > 
> > * Fire pump: 70 psi at 750 GPM, city main supply
> > 
> > * Hydrant flow test not performed, assuming static pressure at street 
> > around 75 psi.
> > 
> > * No standpipe flow information. I recommended a standpipe flow test to be 
> > performed for documentation purposes.
> > 
> >  
> > 
> > Existing Suction Piping
> > 
> > * 4” × 6” concentric reducer at pump suction flange, recommended 
> > replacement with 4” × 6” eccentric reducer
> > 
> > * 1975 water meter to be removed during backflow installation. Couldn’t 
> > find data sheets on this water meter to determine friction loss at system 
> > demand.
> > 
> >  
> > 
> > Pump Test Data
> > 
> >  
> > 
> > Flow
> > 
> > Suction Pressure
> > 
> > Discharge Pressure
> > 
> > Churn
> > 
> > 75 psi
> > 
> > 155 psi
> > 
> > 100% (750 GPM)
> > 
> > 45 psi
> > 
> > 110 psi
> > 
> > 150% (1125 GPM)
> > 
> > 5 psi
> > 
> > 50 psi
> > 
> >  
> > 
> > Sprinkler system demand: 268 GPM at 68 psi
> > 
> > * Light Hazard
> > 
> > * Apartments
> > 
> >  
> > 
> > Concern
> > 
> > * At 150% flow, suction is already 5 psi without a backflow preventer.
> > 
> > * Adding a backflow preventer with additional fittings will introduce 
> > friction loss and will pull city main below zero during high demand.
> > 
> > * Preliminary calculations indicate the standpipe may not achieve 65 psi 
> > residual at 750 GPM; (System installed 1975), verification pending a 
> > standpipe flow test.
> > 
> >  
> > 
> > Questions
> > 
> > 1. If testing confirms the standpipe cannot achieve 65 psi at 750 GPM, what 
> > is the recommended course of action?
> > 
> > 2. How should we address the requirement for a backflow preventer when pump 
> > suction is already low at 150% flow?
> > 
> > 3. Are there alternative design approaches to meet the water authority’s 
> > requirement while maintaining proper pump operation?
> > 
> > 4. Water authority wants the backflow detector assembly on the suction side 
> > of the pump.
> > 
> >  
> > 
> >  
> > 
> > Thank you for any guidance.
> > 
> >  
> > 
> >  
> > 
> >  
> > 
> >  
> > 
> > Thank You,
> > 
> >  
> > 
> > Brett Barrall
> > 
> > Fire Sprinkler Designer
> > 
> > [email protected] mailto:[email protected]
> > 
> >  
> > 
> > [image004.jpg@01D445D6]    
> > 
> >  
> > 
> > 50 S. Museum Road, Reading, PA 19607 https://goo.gl/maps/A3D5Y6oTJUT2
> > 
> > Office: 610-775-1200 ● Toll Free: 1-800-344-4012
> > 
> > www.bsgi.com https://www.berkshiresgi.com/
> > 
> > Satellite Offices in York & State College
> > 
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