The design criteria for CMSA sprinklers in Table 14.3.1 are a carryover from
the 2007 Edition where the requirements were the same for palletized storage
of Class III or Class IV commodities up to a height of 25 ft.  (Check it out
- You need the same number of heads at the same pressure for 20 ft storage
of Class III as for Class IV to 25 ft.)

The equivalent density using CMDA sprinklers for Class IV to 25 ft. is 0.54
fpm/sq ft over 2,000 sq ft. (0.39 from Fig. 14.2.4.1 x height adjustment of
1.38 from Fig. 14.2.4.3).  The flow rate for this arrangement would be 1080
gpm such that going to CMSA would reduce your overall flow for your
situation.  (Using high temp heads would reduce the density to 0.41 gpm/sq
ft, which is similar to what's required for CMSA heads.)

David  

-----Original Message-----
From: [email protected]
[mailto:[email protected]] On Behalf Of J.P. Merlino/
Ing.L.Lagomarsino y Asoc.
Sent: Monday, December 20, 2010 3:44 PM
To: [email protected]
Subject: Class III Solid Pile Protection Criteria

We have doubts regarding criteria for protection of the following:

Class III, solid pile
Storage height: up to 20 ft
Máximum building height 30 ft
NFPA 13 2010 Edition

As we understand, the code gives two options which are:

1) Per 14.2.4, Control Mode Density Area:Figure 14.2.4.2  With ordinary
temperature, K=11,2 sprinkler we need  0,215 gpm/sq ft over 2000 sq ft. Flow
rate equals 430 gpm

2) If we go to 14.3, Control Mode Specific Application, Table 14.3.1, for
same conditions, we are required to have 15 sprinklers with  K= 11,2
operating with a minimum discharge pressure of 25 psi. Flow rate equals 840
gpm and density is 0,43 gpm/sq.ft.

Are both cases valid for the hazard we are protecting?

Why such a large difference in terms of flow and density?

Best regards and thanks in advance

J.P. Merlino
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