The maximum sprinkler demand as per hydraulic calcs. is 222 gpm. The water
supply is by means of storage tanks having a total volume of 7448 gallons.
Just barely enough for approx. 33 minimute at maximum demand. The contractor
has installed a 400 gpm fire pump. NFPA 20 requires gauge pressure at the
fire pump suction flange to be 0 psi or higher when pump is operating at
150% of rated flow, which in this case is 600 gpm. Is this realistic? I
know, if the suction pressure is 0 psi or higher for 600 gpm flow, it will
work for all cases. However, I would expect a flow between the supply and
demand with all design sprinklers flowing. Anyone with experience with
pumps, care to comment?

Tony   

-----Original Message-----
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Joe Hankins
Sent: November 4, 2008 8:56 AM
To: [email protected]
Subject: Re: Fire Pump Suction

 Boiling (cavitation) starts starts when the water pressure at the impeller
is reduced to the vapor pressure of water at the water temperature.  You see
this addressed  in the pump literature as "NPSH" 
The term net positive suction pressure (NPSH) is defined as the difference
between the suction pressure and the vapor pressure of water and must be a
positive number to avoid cavitation. At 68 degrees F water temperature, the
vapor pressure is 0.35 psi. So, as long as the inlet pressure is greater
than 0.35 psi absolute or -14.3 gauge, no cavitation.

In practical terms, so long as the suction pressure is above -12 to -13 psi,
you should be fine.  When a typical centrifugal fire pump starts to
cavitate, you'll know it. (sounds like the pump is full of rocks), and
you're not going to damage the pump unless you let it cavitate for an
extended period of time. The problem, of course, is that the pump
performance deteriorates significantly.

Joe



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