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� <br />� ' � <br />' ***** �FIR$ �SPRINKLER DESIGN PROGRAM BY ELITF SOFTWARE DEVELOPMENT INC ******** <br /> Ci�LWILL FNG,INP$RIN INC. - TAMPA, FL 33605 <br /> WALGRFFsNS 6-28-1999 PAG$ 7 <br /> ***********I********.***** FIRE SPRINKL�R OUTPUT DATA ************************** <br />�I , <br /> OVER.ALL PIPE OUTPUT DATA: � <br />, BFG NODAL� ELEV DISCH. RFS .PR NONIDIA Q(GPM) F.L./FT PIP.L PF-PSI <br /> END K-FAC� (FT) (GPA�!) (PSI) IN.DIA VEL(FPS) FITTINGS FIT.L PB-PSI <br /> I C-VAL TYPPs.GRP TOT.L PV-PSI <br /> �, <br /> 24 N/A' 8 .0 50 .00 43 .62 4 .Q00 404 .7 0 .049 10.0 0.49 <br /> 23 N/A' 18 .0 0 .00 38 . 80 4 .026 10.2 ----- 0 .0 4.33 <br /> SCHFD 40 WET STFFL 120 10 .0 0 .70 <br /> 25 N/A� 3 .0 0 .00 47 .53 4 .000 454 .7 0 .060 5 .0 1.75 <br /> �24 N/A� 8 .0 50 .00 43 .62 4 .026 11.5 GC 24.0 2 .16 <br /> SCHFD 40 WET STEEL 120 29.0 0.88 <br /> � <br /> 26 N/A �� 0 .0 0 .00 49 .82 6 .000 454 .7 0 .006 50.0 1.00 <br /> 25 ' N/A 3 .0 0 .00 47 .53 5.993 5 .2 5F3 123 .,5 1.30 <br /> PVC, �CLASS 200 150 173 .5 0 .18 <br /> i <br /> 26 N/A � 0 .0 0 .00 49 .82 6 .000 -454 .7 0 .006 100 .0 1.08 <br /> 27 N/A � 0 .0 -454 .69 50 .90 5 .993 -5 .2 28T 87 .5 0 .00 <br /> PVC, �CLASS 200 � 150 187 .5 0.18 <br /> I <br /> OVER.ALL SPRI,NKLER OUTPUT DATA: <br /> FLOWING ARFA FLOWING SPRINKL£R RE3IDUAL FLOWING FLOWING SPRINKLSR <br /> SPRINK. GROUP SPRINKLER ELEVATION PRESSURE AREA DENSITY DISCHARGFs <br /> NODP N0. CODE (K FACTOR) ( FEET ) ( PSI ) ( SQFT) (GPM/SQFT) ( GPM ) <br /> I <br />' 1 � 5 .65 18 .00 13 .00 100 .00 0 .204 20 .37 <br /> 2 '� 5 .65 18 .00 14 .62 100 .00 0 .216 21.60 <br /> 3 i 5 .65 18 .00 15 .97 100 .00 0 .226 22 .58 <br /> 4 � 5 .65 18 .00 18 .96 100.00 0.246 24.60 <br /> 5 'I 5 .65 18 ,00 21.52 100 .00 0 .262 26.21 <br /> 7 5 .65 18 .00 13 .32 100 .00 0 .206 20.62 <br /> 8 � 5 .65 18 .00 14 .42 100 .00 0 .215 21.45 <br /> 9 5 .65 18.00 15 .50 100 .00 0 .222 22 .25 <br />, 10 5 .65 18 .00 18 .47 100 .00 0 .243 24.28 <br />� 11 5 .65 18 .00 21.01 100 .00 0 .259 25 .90 <br /> 12 5 .65 18 .00 22 .22 100 .00 0 .266 26.63 <br /> � <br /> �I <br /> I <br /> � <br /> I <br />