Consult the pump manufacturer (if you don't have the information) and find out 
what the minimum acceptable NPSH is for that pump.  It can vary based on pump 
design and selection criteria
but if the suction pressure falls below the mfgrs. NPSH you can end up with 
pump cavitation and destroy the pump.

Craig Prahl | Jacobs | Group Lead/SME – Fire Protection | 864.676.5252 | 
[email protected] | www.jacobs.com
1041 East Butler Road   Greenville, South Carolina  29606

-----Original Message-----
From: Sprinklerforum <[email protected]> On Behalf 
Of Steven Jenkins via Sprinklerforum
Sent: Friday, December 4, 2020 4:57 PM
To: [email protected]
Cc: Steven Jenkins <[email protected]>
Subject: [EXTERNAL] pump suction presure

We have an existing horizontal split case fire pump and ground level water 
storage tank.  The storage in the protected building is changing, and the 
amount of water needed for fire protection is going up.
We are changing the tank to a “break tank”, but even then there is not much 
water left in the tank after the required supply duration, only a few feet left 
in the bottom of the tank.
The pump is right next to the tank, so not much loss due to friction in the 
connecting pipe.
With the tank full, before the pump is turned on, the gauge on the suction side 
reads about 15 psi, due to the height of water in the tank.  When the pump is 
running at 150%, this drops to about 7.5 psi.
At the end of the required duration I will only have about 1.5 psi of head from 
the height of water in the tank.  So if I lose another 7.5 with the pump on, 
the gauge would read -6 psi.
Is this a problem for compliance with 2019 NFPA 20, or since the pump is 
already running does this make the negative 6 psi gauge reading OK?
2019 NFPA 20 4.16.3.2
Thanks,
J
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