Oy vey.   What Chris said.

Steve Leyton
Protection Design & Consulting
San Diego, CA




-----Original Message-----
From: [email protected]
[mailto:[email protected]] On Behalf Of
[email protected]
Sent: Monday, November 30, 2009 12:32 PM
To: [email protected]
Subject: RE: Calcs-How much margin

The test hydrant off the water main runs along a main highway,  the site
is nowhere near this.  I have no data showing any connection between the
little site dwg. provided and a water main on the highway.




Craig L. Prahl, CET   
Fire Protection Specialist
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[email protected]
http://www.ch2m.com 


-----Original Message-----
From: [email protected]
[mailto:[email protected]] On Behalf Of Steve
Leyton
Sent: Monday, November 30, 2009 3:29 PM
To: [email protected]
Subject: RE: Calcs-How much margin

Based on this latest "twist", I would not allow that test to be used as
a basis for the calculation under any circumstances.   Re-take a flow
test off the main that actually serves the system or measure the
friction loss back to the test location through the "several hundred to
a thousand" feet of main that (presumably) exists between the test and
the POC.   Are you even certain it's the same water main system or zone?

Steve Leyton
Protection Design & Consulting
San Diego, CA




-----Original Message-----
From: [email protected]
[mailto:[email protected]] On Behalf Of
[email protected]
Sent: Monday, November 30, 2009 12:23 PM
To: [email protected]
Subject: RE: Calcs-How much margin

They already took the 10% off the available pressures so their actual
margin would be around 10-11 psi without the 10% decrease,  but here's
another twist,  the test hydrant is not on the same water main that
serves the site and is several hundred to a thousand feet away.  So
there is some question as to the real value of the test in relation to
what is actually available at the site.  Calcs say test to riser is less
than 10ft.  


Craig L. Prahl, CET   
Fire Protection Specialist
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[email protected]
http://www.ch2m.com 


-----Original Message-----
From: [email protected]
[mailto:[email protected]] On Behalf Of Steve
Leyton
Sent: Monday, November 30, 2009 3:14 PM
To: [email protected]
Subject: RE: Calcs-How much margin

Did they observe a safety margin below the actual flow test result?   If
you take 10% off the available to start and still have 3.63 PSI, then
sure.  But if that's 3.63 PSI below the actual flow test result then
unless the water supply is ... umm, distressed, it doesn't sound like a
good idea.

Steve Leyton
Protection Design & Consulting
San Diego, CA




-----Original Message-----
From: [email protected]
[mailto:[email protected]] On Behalf Of
[email protected]
Sent: Monday, November 30, 2009 12:11 PM
To: [email protected]
Subject: Calcs-How much margin

I've got a calc I'm reviewing, after all said and done, 3.63 psi margin
between demand and available.  Designer used 4.2K heads to get the flow
exactly to the decimal of the required flow.  This is an industrial type
project.  With a .15 gpm/sf density at 92 sf per head, the flow would be
13.8 gpm and he's dead on the money.  The concern would be that over the
years if there was any change in the water supply or decay of the
piping, that the operation of half the design area would be
questionable.  

Would you approve or reject this design?  Is this cutting it just a bit
close?

 


Craig L. Prahl, CET   
Fire Protection Specialist
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[email protected]
http://www.ch2m.com 

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