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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