I'm not sure I have anything to add, but this is a great anecdote.  I've
don't two flow tests in different parts of San Diego County (different
water purveyors too) where the residual was HIGHER than the static
because of pumps.  And not variable speed, just stand back and watch in
awe as the pressure fell 40-50% and suddenly came charging back to and
beyond the static.  One test was stupefying - the static was 95, which
fell sharply to 75 and then surged up to 120.  I was on the flowing
hydrant and we had one 2.5" flowing straight across a six-lane arterial
street (water department guy didn't trust my diffuser so he wanted to
use his trusty pitot blade.   We shut down and tried it with the 4" port
but it nearly tore his hand off.  Finally put my diffuser back on the
2.5" and got a clean pitot of nearly 100 PSI.   Traffic was a mess,
water everywhere, me laughing like a mental patient.   It was awesome.
Finally decided with the FD to go with 95 static and 90 residual at this
ridiculous flow rate of 1700-something (ridiculous for a 2.5" port, I
mean).    Took 10% off and called it a day.  

Steve Leyton
Protection Design & Consulting
San Diego, CA


-----Original Message-----
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Thom
McMahon
Sent: Saturday, November 29, 2008 1:01 PM
To: [email protected]
Subject: RE: variable public water supply

It sounds like more study for the actual system demand is required,
otherwise your just guessing at the 15 vs. 20 flowing. You'll need to
verify
all start stop settings with the civil engineer for the water purveyor,
and
then look at the system demand, from the flow recorders. What time will
the
system supply/demand be the greatest? This is when your pump will kick
in
fastest. When is the supply/demand the lowest? This is when the pump
will
take longest to kick in, possibly even over the 660 Gpm your system
demands
if when you did your flow test the domestic demand on the system
exceeded
160 Gpm, and your lowest demand is less than 10 Gpm, then it's possible
your
system will never kick the pump in.

Thom McMahon, SET
Firetech, Inc.
2560 Copper Ridge Dr
P.O. Box 882136
Steamboat Springs, CO 80488
Tel:  970-879-7952
Fax: 970-879-7926



-----Original Message-----
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams
Sent: Saturday, November 29, 2008 1:46 PM
To: [email protected]
Subject: RE: variable public water supply

In this case, the new pump is variable speed and is designed to maintain
a
constant pressure. At the hydrant we were reading the pressures on, it
kicked in at 45 psi and boosted it to maintain 65 psi out to the
capacity of
the pump.

My thought is that ignoring the pump at sprinkler flows up to where the
pump
kicked in (approx 500 gpm in this case) is correct. If the system demand
was
over the 500 gpm, what would be the effectiveness of the sprinkler
system at
the flow goes from 0 to whatever the demand is when the curve is not
1.85
linear? From the time of first sprinkler opening, up to the 500 gpm, we
will
be operating on a different flow curve than what we will over the 500
gpm.
Our designs are usually based on a maximum flow requirement only and
assumes
the linearity of the flow curve. Say you have a demand of .30/2000
(ignore
hose streams in this case), or roughly 660 gpm. The sprinklers require
33gpm
each. The design says that we have to calculate 20 sprinklers flowing.
Should the design for the first 15 sprinklers (.30/1500) be based on the
lesser curve and the .30/2000 be based on the curve with the pump? Two
sets
of calcs? How do you justify this to the septic system engineer that
speced
out the sprinkler system?



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