I am coordinating a flow test with a contractor.
NFPA 291 Section 4.4.6 states "To obtain satisfactory test results of theoretical calculation of expected flows or rated capacities, sufficient discharge should be achieved to cause a drop in pressure at the residual hydrant of at least 10 percent. In water supply systems where additional municipal pumps increase the flow and pressure as additional test hydrants are opened, it might be necessary to declare an artificial drop in the static pressure of 10 percent to create a theoretical water supply curve." The contractor did not achieve the 10% pressure drop and asked if the "artificial pressure drop" option is a possibility here. I do not see anywhere in NFPA 291 or elsewhere explaining how to do this. Any recommendations on what to advise the contractor / how to even calculate the artificial pressure drop? Thanks in advance. Sent in anonymously for discussion. Click Title to View | Submit Your Question | Subscribe
14 Comments
Pete H
6/26/2024 06:51:27 am
I can be entirely wrong about this, but I'm pretty sure you just make sure your residual is 10% less than your static.
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Glenn Berger
6/26/2024 08:12:16 am
Do not attempt to "create" an artificial pressure drop.
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Eric R
6/26/2024 08:18:36 am
Glenn,
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Dan Wilder
6/26/2024 08:12:48 am
As long as the discharge flow meets or exceeds the demand of the system being installed, Pete has it correct by dropping the residual by the needed 10%. Also, this 10% reduction should be independent of any additional safety factor required/requested for the system calculations.
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Eric R
6/26/2024 08:13:14 am
Pete is correct on this.
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Joe
6/26/2024 08:14:55 am
Such an interesting way of going about it - the gauge inaccuracy is a huge compounding factor here.
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Bob
6/26/2024 08:15:58 am
To get the artificial 10% pressure drop you would use the same formula that you do for the 20psi calculation. Calculation is found in 291 4.13.1.2
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Jesse
6/26/2024 09:55:11 am
291 is an interesting document because its a recommended process.
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Jack G
6/26/2024 11:01:18 am
I m with Dan and Glenn on this.
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Casey Milhorn
6/26/2024 05:30:38 pm
I completely disagree with this "suggestion" in NFPA 291. I think it should be replaced with "your gpm achieved during the flow test must match, at minimum, the gpm required in the most demanding calculation". I'm more worried about achieving enough flow than achieving a certain "drop" in pressure. Too many times designers are designing fire pumps based on points out on the curve where actual results weren't achieved.
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Eric R
6/27/2024 07:09:39 am
Casey,
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Casey Milhorn
6/27/2024 07:29:52 am
Thanks Eric. Yeah, I understand the reasoning for this "safety margin" but I don't agree with the approach. Most AHJs and/or engineers specs we see, ask for a 5% or 10% (or even more) safety margin. Even when this is not required, I've taught all of my designers to never design right to the edge of the supply. Factoring in a safety margin across the curve makes more sense. In a light hazard scenario, we are typically working right up against the static pressure and regardless of the 10% drop across the flow at residual, you don't get any safety margin benefit up top. If you've ever taken flow tests at different times of day, or on different days, you can see a drastic change in static pressure in some city systems, which usually has a drastic change on the residual side as well. Flow of course has some correlation to static and residual pressure, but also with overall system capacity. That being said, I worry more about applying an overall safety margin across the curve and also ensuring that the actual water flowed during the test is more than the anticipated system demand and the designer isn't working in "theoretical" residuals and flows. Achieving a 10% drop on the residual side of the curve makes no sense unless you are working out past your residual point in anticipated flow demand.
AW
6/26/2024 07:53:22 pm
Can you do a 24 Hour Static Test instead?
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Mark Harris
6/29/2024 08:00:03 am
Fire Marshal Association in my market requires a 20% safety factor but need to take the static adjustment to both static and residual so the available supply curve is still parallel to the flow test. For example a 100 static 80 residual 10,000 GPM actual flow test would be 84 static and 64 residual.
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