But if only one head activates, there is not much of an emergency, no?

Brad
On Jan 17, 2017 7:53 PM, "Timothy Goins" <[email protected]> wrote:

> Fine and good into you have a fire with only one had that activates.
>
> Therefore I say unto you, Take no thought for your life, what ye shall
> eat, or what ye shall drink; nor yet for your body, what ye shall put on.
> Is not the life more than meat, and the body than raiment?
> MAT 6:25
>
> Jesus answered, Verily, verily, I say unto thee, Except a man be born of
> water and of the Spirit, he cannot enter into the kingdom of God. JHN 3:5
>
> On Jan 17, 2017, at 3:16 PM, Steve Leyton <[email protected]>
> wrote:
>
> Okay, great and wonderful but you what that does is flatten the curve and
> potentially makes higher flow rate residual pressures plot HIGHER than they
> would otherwise be.   Soooooooo … as a designer-of-record charged with
> (among myriad other things) anticipating worst case scenario, methinks it
> makes sense to keep as much tilt in that flow data curve as possible.
>
>
>
> Steve L.
>
> (My opinion only, based on numerous cases served as an expert witness and
> somebody who buys a lot of liability insurance every year.)
>
>
>
> *From:* Sprinklerforum [mailto:[email protected].
> org <[email protected]>] *On Behalf Of *Dewayne
> Martinez
> *Sent:* Tuesday, January 17, 2017 1:13 PM
> *To:* [email protected]
> *Subject:* RE: Static pressure after backflow preventer
>
>
>
> Ames got back to me and said “Yes there is a pressure loss at static
> flow. It will depend on which type backflow youre looking at. A RPZ will
> usually show a 10-15 PSI drop. A double check is usually 8-10.”
>
>
>
>
>
> *From:* Sprinklerforum [mailto:[email protected].
> org] *On Behalf Of *Brad Casterline
> *Sent:* Thursday, January 12, 2017 12:51 PM
> *To:* [email protected]
> *Subject:* RE: Static pressure after backflow preventer
>
>
>
> Matt,
>
>
>
> I think your example of sliding friction is excellent. Pressure is force
> divided by area, and force is mass times acceleration.
>
> With sliding friction the force required to give a mass an acceleration is
> greater than the force required to keep it going a constant velocity.
>
> With fluid friction viscosity comes into play and is actually related to
> sliding friction in that the constant force required to slide a steel plate
> across the surface of a fluid, imparting a certain constant velocity to the
> plate is a measure of the viscosity of the fluid.
>
>
>
> But the question is regarding friction loss when the flow is 0 GPM, and at
> 0 GPM the velocity of the water = 0.
>
> Near the end of what I pasted you see:
>
> mgh=1/2mv^2.
>
> This is the Conservation of Energy formula for going from Potential Energy
> (static), to Kinetic Energy (residual).
>
> In a closed system no mass is gained or lost (it is the same on both sides
> so it cancels out), so,
>
> h=v^2/2g, and,
>
> v=SQRT(2gh).
>
> But if the velocity is 0 on both sides the only way to get a different
> force measurements is with different h measurements (elevations).
>
>
>
> I know you and others know all this, so please excuse my didactic tone.
>
>
>
> Brad
>
>
>
> <image001.jpg>
>
> <image002.jpg>
>
>
> ------------------------------
>
> *From:* Sprinklerforum [mailto:[email protected].
> org <[email protected]>] *On Behalf Of *Matt
> Grise
> *Sent:* Thursday, January 12, 2017 6:33 AM
> *To:* [email protected]
> *Subject:* RE: Static pressure after backflow preventer
>
>
>
> Of course – if you are super close to a pressure limit – the BFP might
> also lock in some unusually high pressure spike that occurs in the system.
> Then the sprinkler system could sit around locked at a pressure that is
> greater than even the typical measured static.
>
>
>
> Matt
>
>
>
>
>
> *From:* Sprinklerforum [mailto:[email protected].
> org <[email protected]>] *On Behalf Of *Matt
> Grise
> *Sent:* Thursday, January 12, 2017 6:30 AM
> *To:* [email protected]
> *Subject:* RE: Static pressure after backflow preventer
>
>
>
> Just to think out loud – I don’t have a perfect understanding of how very
> low flow works through backflows… but:
>
>
>
> It seems like the system static that is locked in is usually pretty close
> to the flow test static. I wonder if the noticeable pressure loss to
> initially open the BFP, that goes down once flow starts, if that pressure
> drop might approach zero as the flow goes from positive back to zero.
>
>
>
> That is – the pressure drop seen at a flow that is just barely over zero
> depends on whether you are approaching that flow from zero, or from [more
> than zero].
>
>
>
> For example: if you slide a block across a table – the force it takes to
> move the block at a very low speed will depend a lot on whether you start
> from a standstill, or a faster speed. (that illustrates a different
> principle, but shows how the approach could change)
>
>
>
> Thoughts?
>
>
>
> Matt
>
>
>
> *From:* Sprinklerforum [mailto:[email protected].
> org <[email protected]>] *On Behalf Of *Roland
> Huggins
> *Sent:* Wednesday, January 11, 2017 6:07 PM
> *To:* SprinklerFORUM
> *Subject:* Re: Static pressure after backflow preventer
>
>
>
> I'm flying by the seat of my pants (with no lights) but until I prove to
> myself otherwise (or am beat into submission by the technical committee), I
> don’t see why we should beat ourselves up and default to what ever seems to
> be the most conservative.  Our supply curve is a straight line relationship
> from static to some lower residual pressure.  We now incorporate a device
> that has a crazy high initial pressure loss that then drops back into a
> more normal curve.  In looking at SYSTEM DEMAND are we well served by
> ignoring the actual available pressure that was otherwise lost due to
> accounting for a wiggle at the front end.
>
>
>
>  For now, I’ll stick with my mantra:  Lead the way, Mr. Custer. I’m right
> behind you.
>
>
>
>
>
> Roland Huggins, PE - Senior VP Engineering
>
> American Fire Sprinkler Assn.
>
> Dallas, TX
>
> http://www.firesprinkler.org
>
>
>
> Fire Sprinklers Saves Lives
>
>
>
>
>
>
>
>
>
> On Jan 11, 2017, at 12:27 PM, Dewayne Martinez <
> [email protected]> wrote:
>
>
>
> I have used the static without the backflow loss in the past but I noticed
> with the SprinkCad software I am running it uses the mfg curves and it was
> showing less static than I had figured.  If I take into account the BFP
> loss I can eliminate 6 pressure reducing hose valves…..Looks like I will
> err on the side of caution and design them in.
>
> Thanks,
>
> Dewayne
>
>
>
>
>
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