Well with that said there is no way to approve even with 30 psi CALC'ED
safety.  GIGO...If you don't have the right test you don't know which side
of the curve you are on.  Sure, bigger mains, down hill you can make some
educated guesses.

Not approved! 

Chris 

-----Original Message-----
From: [email protected]
[mailto:[email protected]] On Behalf Of
[email protected]
Sent: Monday, November 30, 2009 2:23 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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