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AREA 1 CALCUATION
Hydraulic calculations using HydraCALC CORNELIUSEN CONSULTING 20 HIDDEN MEADOWS LANE WRENTHAM MASS 02093 781-248-7497 Job Name : 217 ESSEX STREET SPRINKLER SYSTEM REV A Drawing : SP-1 TO 5 Location : 217 -221 ESSEX STREET SALEM Remote Area : AREA 1 Contract Data File : 217 ESSEX STREET SPRINKLER SYSTEM REV A Area 1.WXF Computer Programs by Hydratec Inc. Revision: 50.53.5 Water Supply Curve C water Supply Demand: :;s1 - Static Pressure 70 D1 - Elevation - Residual Pressure: 67 D2 - System Flow : 63.203 - Residual Flow : 811 D2 - System Pressure : 25.846 Hose ( Demand) : 100 D3 - System Demand : 163.203 Safety Margin : 44.000 0 C m 1 O 0 �7 0 CD 0 N 0 0 0 0 0 CD 0 0 0 0 co O ic) V M N W U) U) D W 0 CO 0 0 0 0 0 0 M 0 Z 0 -J LL. Revision: 50.53.5 Computer Programs by Hydratec Fittings Used Summary / og CO CO m oE CN. .t = m£/ RR )Co CV C04 \ o= »2 c @ E) w @ 0 .5 / »2 «°2�c r w E ƒ § 2 .g 9O�»\ 10=ifs \ -w= /2 ®ca�u =03C0 TO 0 0 \f % CD, k m (00%c0 c (Ea) ƒ 0 0 5 9 2 a c Z _ _ > u- 0 \ E2 /,. 2 E o«=«== �t°�k? \ 0 at co_c13 or=wCD= 5£ w0C0�mg « $ c - a) = m _ 5 % ƒ « « = c 0CV2OU)2 a)$ �E£k/f 2 $ 0_ ® _c.cli 2 2 @\ /2 7 EF 2 0C§0V'E 2O _%' a« \ \ 2_0c EaE202 = m = ' w 2 « a o-\on§ /ƒ/a 727\E( e c2e .>7oc- 2 $a/2\& % cn kca N§E\ k7«\\ %k%>22)® 5c /c/ -f{/ a_c222E&tm;t, t%5m =�o�oa 45 \=a5ma)) oc_a e2272»R w w 232E=° =t §ƒƒ\ƒƒ$ a 2 f �/ £� Cl) \co m1LU2L�E E _._ 0�@>�� z azz=zz< E / /� =cy£§3 £» ƒ_/§ �f°7// >o.�� f/ » DER$ �52�.&0 ik 2=wLLmwN \ J ± ƒ 0_ Z PT ' / Flow Summary - NFPA CORNELIUSEN CONSULTING 217 ESSEX STREET SPRINKLER SYSTEM REV A Page 3 Date Node at Static Residual Source Pressure Pressure SUPPLY ANALYSIS Available Flow Pressure Total Demand Required Pressure TEST 70.0 67 811.0 69.845 163.2 25.846 NODE ANALYSIS Pressure Discharge Node Tag Elevation Node Type at Node at Node Notes B400 0.0 4.2 11.76 14.4 B401 0.0 11.78 B402 0.0 11.83 B405 0.0 12.2 B407 0.0 12.83 M408 0.0 15.35 M407 0.0 15.99 M406 0.0 16.05 M405 0.0 16.45 M404 0.0 16.65 M403 0.0 16.75 FC10 0.0 21.1 400 0.0 21.67 105 0.0 21.9 B-5 8.0 18.46 M106 8.0 18.49 M105 8.0 18.57 M104 8.0 18.58 M103 8.0 18.59 M102 8.0 18.61 M101 8.0 18.64 M100 8.0 18.68 100 8.0 18.68 RA11 8.0 18.75 RA10 3.0 20.92 BF13 3.0 20.94 BF12 3.0 20.95 BF11 3.0 24.45 BF10 3.0 24.47 UG10 3.0 24.5 UG11 0.0 25.82 HOSE 0.0 25.84 100.0 TEST 0.0 25.85 B403 0.0 4.9 11.72 16.78 B404 0.0 4.9 12.09 17.03 B406 0.0 4.2 12.74 14.99 Computer Programs by Hydratec Inc. Revision: 50.53.5 Final Calculations : Hazen -Williams CORNELIUSEN CONSULTING 217 ESSEX STREET SPRINKLER SYSTEM REV A Page 4 Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe Node2 Elev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf ******* Notes ****** 6400 0 4.20 14.40 1.5 0.0 2.450 120 11.755 to 0.0 0.0 0.0 B401 0 14.4 1.61 0.0 2.450 0.0090 0.022 Vel = 2.27 B401 0 0.0 1.5 E 4.0 2.500 120 11.777 to 0.0 4.000 0.0 B402 0 14.4 1.61 0.0 6.500 0.0088 0.057 Vel = 2.27 B402 0 16.78 1.5 0.0 10.000 120 11.834 to 0.0 0.0 0.0 B405 0 31.18 1.61 0.0 10.000 0.0367 0.367 Vel = 4.91 B405 0 17.03 1.5 0.0 7.610 120 12.201 to 0.0 0.0 0.0 B407 0 _ 48.21 1.61 0.0 7.610 0.0823 0.626 Vel = 7.60 B407 0 14.99 1.5 T 8.0 10.580 120 12.827 to 0.0 8.000 0.0 M408 0 63.2 _ 1.61 0.0 18.580 0.1358 2.523 Vel = 9.96 M408 0 0.0 2 0.0 19.560 120 15.350 to 0.0 0.0 0.0 M407 0 63.2 2.157 0.0 19.560 0.0327 0.639 Vel = 5.55 M407 0 0.0 2 0.0 1.780 120 15.989 to 0.0 0.0 0.0 M406 0 _ 63.2 2.157 0.0 1.780 0.0326 0.058 Vel = 5.55 M406 0 to M405 0 M405 0 to M404 0 M404 0 to M403 0 0.0 2 63.2 2.157 0.0 2 63.2 2.157 0.0 2 63.2 2.157 0.0 12.360 120 16.047 0.0 0.0 0.0 0.0 12.360 0.0327 0.404 Vel = 5.55 0.0 6.150 120 16.451 0.0 0.0 0.0 0.0 6.150 0.0327 0.201 Vel = 5.55 0.0 2.940 120 16.652 0.0 0.0 0.0 0.0 2.940 0.0327 0.096 Vel = 5.55 M403 0 0.0 2 T 12.307 8.260 120 16.748 to S 13.537 33.228 3.000 * * Fixed Loss = 3 FC10 0 63.2 2.157 Fsp 0.0 41.488 0.0327 1.355 Vel = 5.55 B 7.384 FC10 0 0.0 2 E 6.153 11.220 120 21.103 to 0.0 6.153 0.0 400 0 _ 63.2 2.157 0.0 17.373 0.0327 0.568 Vel = 5.55 400 0 0.0 2 E 6.153 1.000 120 21.671 to 0.0 6.153 0.0 105 0 63.2 2.157 0.0 7.153 0.0326 0.233 Vel = 5.55 105 0 0.0 4 E 13.167 0.820 120 21.904 to 0.0 13.167 -3.465 6-5 8 63.2 4.26 _ 0.0 13.987 0.0012 0.017 Vel = 1.4.2 6-5 8 0.0 4 E 13.167 14.740 120 18.456 to 0.0 13.167 0.0 M106 8 _ 63.2 4.26 0.0 27.907 0.0012 0.033 Vel = 1.42 M106 8 0.0 4 E 13.167 56.530 120 18.489 to 0.0 13.167 0.0 M105 8 63.2 4.26 0.0 69.697 0.0012 0.083 Vel = 1.42 Computer Programs by Hydratec Inc. Revision: 50.53.5 Final Calculations : Hazen -Williams CORNELIUSEN CONSULTING 217 ESSEX STREET SPRINKLER SYSTEM REV A Page 5 Date Nadel Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe Node2 Elev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf ******* Notes ****** M105 8 0.0 4 0.0 4.530 120 18.572 to 0.0 0.0 0.0 M104 8 63.2 4.26 0.0 4.530 0.0013 0.006 Vel = 1.42 M104 8 0.0 4 E 13.167 0.660 120 18.578 to 0.0 13.167 0.0 M103 8 63.2 4.26 0.0 13.827 0.0012 0.016 Vel = 1.42 M103 8 0.0 4 E 13.167 1.000 120 18.594 to 0.0 13.167 0.0 M102 8 63.2 4.26 0.0 14.167 0.0012 0.017 Vel = 1.42 M102 8 0.0 4 2E 26.334 0.660 120 18.611 to 0.0 26.334 0.0 M101 8 63.2 4.26 0.0 26.994 0.0012 0.032 Vel = 1.42 M101 8 0.0 4 T 26.334 2.210 120 18.643 to 0.0 26.334 0.0 M100 8 63.2 4.26 0.0 28.544 0.0012 0.034 Vel = 1.42 M100 8 0.0 4 0.0 1.560 120 18.677 to 0.0 0.0 0.0 100 8 63.2 4.26 0.0 1.560 0.0013 0.002 VeI = 1.42 100 8 0.0 4 E 13.167 0.520 120 18.679 to Aty 30.284 59.251 0.0 RA11 8 63.2 4.26 B 15.8 59.771 0.0012 0.071 Vel = 1.42 RA11 8 0.0 4 0.0 5.000 120 18.750 to 0.0 0.0 2.166 RA10 3 63.2 4.26 0.0 5.000 0.0010 0.005 Vel = 1.42 RA10 3 0.0 4 E 13.167 1.000 120 20.921 to 0.0 13.167 0.0 BF13 3 63.2 4.26 0.0 14.167 0.0012 0.017 VeI = 1.42 BF13 3 0.0 4 E 13.167 1.000 120 20.938 to 0.0 13.167 0.0 BF12 3 63.2 4.26 0.0 14.167 0.0012 0.017 Vel = 1.42 BF12 3 0.0 4 E 13.167 1.000 120 20.955 to Zac 0.0 13.167 3.480 * * Fixed Loss = 3.48 BF11 3 63.2 4.26 0.0 14.167 0.0012 0.017 Vel = 1.42 BF11 3 0.0 4 E 13.167 1.000 120 24.452 to 0.0 13.167 0.0 BF10 3 63.2 4.26 0.0 14.167 0.0011 0.016 Vel = 1.42 BF10 3 0.0 4 2E 26.334 1.000 120 24.468 to 0.0 26.334 0.0 UG10 3 63.2 4.26 0.0 27.334 0.0012 0.033 Vel = 1.42 UG10 3 0.0 4 E 13.167 3.000 120 24.501 to 0.0 13.167 1.299 UG11 0 63.2 4.26 0.0 16.167 0.0012 0.019 VeI = 1.42 UG11 0 0.0 6 E 20.084 100.000 140 25.819 to 0.0 20.084 0.0 HOSE 0 63.2 6.16 0.0 120.084 0.0001 0.018 Vel = 0.68 HOSE 0 H100 100.00 12 0.0 300.000 140 25.837 to 0.0 0.0 0.0 TEST 0 163.2 12.34 0.0 300.000 0 0.009 VeI = 0.44 Computer Programs by Hydratec Inc. Revision: 50.53.5 Final Calculations : Hazen -Williams CORNELIUSEN CONSULTING 217 ESSEX STREET SPRINKLER SYSTEM REV A Page 6 Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe Node2 Elev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf Notes ****** 0.0 TEST 163.20 _ 25.846 K Factor = 32.10 B403 0 4.90 16.78 1.5 T 8.0 1.650 120 11.721 to 0.0 8.000 0.0 B402 0 _ 16.78 1.61 0.0 9.650 0.0117 0.113 Vel = 2.64 0.0 B402 16.78 11.834 K Factor = 4.88 B404 0 4.90 17.03 1.5 T 8.0 1.650 120 12.085 to 0.0 8.000 0.0 B405 0 17.03 1.61 0.0 9.650 0.0120 0.116 Vel = 2.68 0.0 B405 17.03 _ 12.201 K Factor = 4.88 B406 0 4.20 14.99 1.5 T 8.0 0.800 120 12.744 to 0.0 8.000 0.0 B407 0 14.99 1.61 0.0 8.800 0.0094 0.083 Vel = 2.36 B407 0.0 14.99 12.827 K Factor = 4.19 Computer Programs by Hydratec Inc. Revision: 50.53.5