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HomeMy WebLinkAbout295 Rye Street - Building Plans &amp; Drawin (5) S. A. COMUNALE Page 1 SYSTEM 1 Date 7.6.18 Hvdraulic Desian Information Sheet Name - ALDI'S SOUTH WINDSOR DRY EXPANSION Date - 7.6.18 Location - 295 RYE ST, SOUTH WINDSOR, CT, 06074 Building - System No. - 1 Contractor - S. A. COOMUNALE Contract No. - 58056-018 -Calculated By - A SMITH Drawing No. - 3 OF 5 Construction: ( } Combustible (X) Non-Combustible Ceiling Height - 39'-0" Occupancy - HIGH -PILED STORAGE S (X) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y { i Figure Curve S Other HIGH-PILED STORAGE T Specific Ruling Made By Date E M Number of ESFR Sprinklers - 12 System Type Sprinkler/Nozzle End Head Pressure (PSI) - 52 (X) Wet Make RELAIBLE D ESFR K-Factor - 16.8 { ) Dry Model JL-17 E Elevation at Highest Outlet - 38'-0" ( ) Deluge Size IN" S Hose Allowance - Inside - 100 ) Preaction K-Factor 16.8 I Rack Sprinkler Allowance - ( } Other Temp.Rat.165° G Hose Allowance - Outside - 150 N Note Calculation Flow Required - 1713.1 Press Required - 155.5 AT PUMP DISCHARGE Summary C-Factor Used: 120 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - Cap. - T Time of Test - Rated Cap.- 2000 Elev.- E Static Press - @ Press - 160 R Residual Press - Elev. - 2 Well Flow - Proof Flow S Elevation - U P Location - NEW PUMP AND 250,000 GALLON WATER STORAGE TANK P L Source of Information - Y C Commodity GROUP A U.E.P. Class I-IV Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled Palletized Rack M Single Row { ) Conven. Pallet ( ) Auto. Storage ( ) Encao. S R ( ) Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( } Mult. Row ( } Open Shelf 0 C _ R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse \Wti��tuununrrpp Horizontal Barriers Provided: — — a��Q�P�"R•'�O fi,��y • to: '•.��' 27160 >y �9tn�4NN I 1 1 I i i Water Supply Curve C S. A. COMUNALE Page 2 SYSTEM 1 Date 7.6.18 Pump Data: Demand: P1 - Pump Churn Pressure 177 D1 - Elevation 15.592 P2- Pump Rated Pressure 160 D2-System Flow : 1463.07 P2 - Pump Rated Flow 2000 D2 -System Pressure : 155.536 P3 - Pump Pressure @ Max Flow 120 Hose( Demand ) : 250 P3 - Pump Max Flow 3750 D3-System Demand : 1713.07 Safety Margin 9.291 180 Pi 168 P2 156 2 P 144 R 132 E 120 P3 S 108 S 96 U 84 R 72 E 60 48 36 24 12MA 400 800 1200 1600 2000 2400 2800 3200 3600 FLOW( NA1.85 ) ComP_iter Programs by Hydratec Inc. Revision: 50.52.1 Fittings Used Summary S. A. COMUNALE Page 3 SYSTEM 1 Date 7.6.18 Fitting Legend Abbrev. Name '/2 3/4 1 1a 1'/2 2 21i2 3 3'/z 4 5 6 8 10 12 14 16 18 20 24 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 (p 10 12 19 21 0 0 0 0 0 F NFPA 13 45'Elbow 1 1 1 1 2 2 3 3 3 4 15 7 9 11 13 17 19 21 24 28 G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 L NFPA 13 Long Turn Elbow 0.5 1 2 2 2 3 4 5 5 6 �8 9 13 16 18 24 27 30 34 40 S NFPA 13 Swing Check 0 0 5 7 9 11 14 16 19 22 �27 32 45 55 65 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 10 12 15 17 20 125 30 35 50 60 71 81 91 101 121 V 90'EII Firelock#001 0 0 0 0 0 3.5 4.3 5 +J 6.8 18.5 10 13 4.5 5.1 0 0 0 0 0 X 90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 i21 25 33 9.3 11 0 0 0 0 0 Unit Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *. The fittings marked with a*show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a*will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Revision: 50.52.1 Pressure / Flow Summary- STANDARD S. A. COMUNALE Page 4 SYSTEM 1 Date 7.6.18 Node Elevation K-Fact Pt Pn Flow Density Area Press No•_ ___ Actual Actual _ Rem 1 38.0 77.3 na 2 38.0 71.81 na 3 38.0 16.8 52.92 na 122.21 0.2 85.5 52.0 4 38.0 16.8 52.0 na 121.15 0.2 85.5 52.0 5 38.0 16.8 52.0 na 121.15 0.2 85.5 52.0 6 38.0 16.8 53.04 na 122.35 0.2 85.5 52.0 7 38.0 71.29 na 9 38.0 77.43 na 10 38.0 71.93 na 11 38.0 16.8 53.02 na 122.33 0.2 85.5 52.0 12 38.0 16.8 52.09 na 121.26 0.2 85.5 52.0 13 38.0 16.8 52.1 na 121.26 0.2 85.5 52.0 14 38.0 16.8 53.14 na 122.47 0.2 85.5 52.0 15 38.0 71.42 na 17 38.0 77.91 na 18 38.0 72.38 na 19 38.0 16.8 53.36 na 122.72 0.2 85.5 52.0 20 38.0 16.8 52.44 na 121.65 0.2 85.5 52.0 21 38.0 16.8 52.44 na 121.65 0.2 85.5 52.0 22 38.0 16.8 53.49 na 122.87 0.2 85.5 52.0 23 38.0 71.89 na 25 38.0 78.92 na 26 38.0 78.92 na 27 38.0 78.87 na 29 38.0 79.95 na 30 38.0 79.95 na 31 38.0 79.93 na 33 38.0 80.92 na 34 38.0 80.92 na 35 38.0 80.91 na 37 38.0 81.98 na 38 38.0 81.98 na 39 38.0 81.98 na 41 38.0 83.05 na 42 38.0 83.05 na 43 38.0 83.05 na 45 38.0 84.11 na 46 38.0 84.11 na 47 38.0 84.11 na 49 38.0 85.18 na 50 38.0 85.18 na 51 38.0 85.18 na 53 38.0 86.22 na 54 38.0 86.22 na 55 38.0 86.22 na 57 38.0 87.27 na 58 38.0 87.27 na 59 38.0 87.27 na 61 38.0 88.32 na 62 38.0 88.32 na 63 38.0 88.32 na 65 38.0 89.36 na 66 38.0 89.36 na 67 38.0 89.37 na 69 3&0 90.4 na 70 38.0 90.4 na 71 38.0 90.42 na 73 38.0 91.44 na 74 38.0 91.44 na 75 38.0 91.48 na 77 38.0 92.45 na 78 38.0 92.46 na Computer Programs by Hydratec Inc. Revision: 50.52.1 Flow Summary - Standard S. A. COMUNALE Page 5 SYSTEM 1 Date 7.6.18 Node Elevation K-fact Pt r-n Row vcnSity Area Press No. Actual Actual Reg. 79 38.0 92.55 na 81 38.0 93.45 na 82 38.0 93.47 na 83 38.0 93.64 na 85 38.0 94.42 na 86 38.0 94.46 na 87 38.0 94.75 na S9 38.0 95.35 na 90 38.0 95.41 na 91 38.0 95.9 na 93 38.0 96.23 na 94 38.0 96.32 na 95 38.0 97.09 na 97 38.0 97.05 na 98 38.0 97.18 na 99 38.0 98.35 na 101 38.0 97.79 na 102 38.0 97.99 na 103 38.0 99.69 na 105 38.0 98.45 na 106 38.0 98.73 na 109 38.0 99.01 na 110 38.0 99.41 na 111 38.0 102.74 na 113 38.0 99.46 na 114 38.0 100.0 na 115 38.0 104.51 na 117 38.0 99.8 na 118 38.0 100.51 na 119 38.0 106.49 na 121 38.0 100.02 na 122 38.0 100.95 na 123 38.0 108.73 na 125 38.0 100.14 na 126 38.0 101.32 na 127 38.0 111.3 na 129 38.0 100.18 na 130 38.0 101.67 na 131 38.0 114.28 na 8 38.0 77.14 na 16 38.0 77.28 na 24 38.0 77.78 na 28 38.0 78.86 na 32 38.0 79.93 na 36 38.0 80.91 na 40 38.0 81.98 na 44 38.0 83.05 na 48 38.0 84.11 na 52 38.0 85.18 na 56 38.0 86.22 na 60 38.0 87.27 na 64 38.0 88.32 na 68 38.0 89.37 na 72 38.0 90.42 na 76 38.0 91.48 na 80 38.0 92.56 na 84 38.0 93.66 na 88 38.0 94.78 na 92 38.0 95.95 na 96 38.0 97.18 na i 100 38.0 98.49 na i 1 ( Computer Programs by Hydratec Inc. Revision: 50.52.1 I Flow Summary - Standard S. A. COMUNALE Page 6 SYSTEM 1 Date 7.6.18 Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual 104 38.0 99.89 na 108 38.0 101.42 na 112 38.0 103.14 na 116 38.0 105.04 na 120 38.0 107.2 na 124 38.0 109.65 na 128 38.0 112.48 na 132 38.0 115.77 na FMJ 38.0 116.56 na TR1 38.0 130.5 na BR1 2.0 151.32 na 100.0 LI 2.0 152.13 na UG 2.0 154.68 na 150.0 PO 2.0 155.54 na The maximum velocity is 32.93 and it occurs in the pipe between nodes 132 and FMJ Computer Programs by Hydratec Inc. Revision: 50.52.1 EOD S. A. COMUNALE Page 7 SYSTEM 1 Date 7.6.18 Node! Elev1 K Qa Nom Fitting Pipe CFact Pi to Or Ftng's Pe * *** Notes *****k Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 1 38 -239.37 2 T 12.307 2.000 120 77.298 to 0.0 12.307 0.0 2 38 -239.37 2.157 0.0 14.307 -0.3838 -5.491 Vel = 21.02 2 38 0.0 2 X 10.461 38.750 120 71.807 to 0.0 10.461 0.0 3 38 -239.37 2.157 0.0 49.211 -0.3838 -18.886 Vel= 21.02 3 38 16.80 122.22 2 0.0 9.000 120 52.921 to 0.0 0.0 0.0 4 38 _ -117.15 2.157 0.0 9.000 -0.1023 -0.921 Vel= 10.29 4 38 16.80 121.14 2 0.0 9.000 120 52.000 to 0.0 0.0 0.0 5 38 _3.99 2.157 0.0 9.000 0.0002 0.002 Vel= 0.35 5 38 16.80 121.15 2 0.0 9.000 120 52.002 _ to 0.0 0.0 0.0 6 38 16.80 122.36 2 X 10.461 34.250 120 53.042 to 0.0 10.461 0.0 _7 38 247.5 2.157 0.0 44.711 0.4082 18.253 Vel = 21.73 7 38 0.0 2 T 12.307 2.000 120 71.295 to 0.0 12.307 0.0 8 38 247.5 2.157 0.0 14.307 0.4082 5.840 Vel = 21.73 0.0 8 247.50 77.135 K Factor= 28.18 9 38 239.56 2 T 12.307 2.000 120 77.430 to 0.0 12.307 0.0 10 38 -239.56 2.157 0.0 14.307 -0.3844 -5.499 Vel= 21.03_ _ 10 38 0.0 2 X 10.461 38.750 120 71.931 to 0.0 10.461 0.0 11 38 -239.56 2.157 0.0 49.211 -0.3843 -18.914 Vel = 21.03 11 38 16.80 122.32 2 0.0 9.000 120 53.017 to 0.0 0.0 0.0 12 38 -117.24 2.157 0.0 _ 9.000 -0.1026 -0.923 Vel= 10.29 12 38 16.80 121.26 2 0.0 9.000 120 52.094 to 0.0 0.0 0.0 13 38 4.02 2.157 0.0 9.000 0.0002 0.002_ Vel= 0.35 13 38 16.80 121.26 2 0.0 9.000 120 52.096 to 0.0 0.0 0.0 14 38 125.28 2.157 0.0 9.000 0.1159 1.043 Vel = 11.00 14 38 16.80 122.46 2 X 10.461 34.250 120 53.139 to 0.0 10.461 0.0 15 38 247.74 2.157 0.0 _44.711 0.4090 18.286 Vel = 21.75 _ 15 38 0.0 2 T 12.307 2.000 120 71.425 to 0.0 12.307 0.0 16 38 247.74 2.157 0.0 _ 14.307 0.4090 5.851_ Vel= 21.75 0.0 16 _ _ 247.74 _ _ 7_276 _ K Factor= 28.18 17 38 -240.27 2 T 12.307 2.000 120 77.908 to 0.0 12.307 0.0 18 38 -240.27 2.157 0.0 14.307 -0.3865 -5.529 Vel = 21.10 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 8 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ****'* Notes * ** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 18 38 0.0 2 X 10.461 38.750 120 72.379 to 0.0 10.461 0.0 19 38 -240.27 2.157 0.0 49.211 -0.3864 -19.017 Vel = 21.10 19 38 16.80 122.73 2 0.0 9.000 120 53.362 to 0.0 0.0 0.0 20 38 -117.54 2.157 0.0 9.000 -0.1029 -0.926 Vel = 10.32_ 20 38 16.80 121.65 2 0.0 9.000 120 52.436 to 0.0 0.0 0.0 21 _ 38 4.11 2.157 0.0 9.000 0.0001 0.001 Vel = 0.36 21 38 16.80 121.65 2 0.0 9.000 120 52.437 to 0.0 0.0 0.0 22 38 125.76 2.157 0.0 9.000 0.1167 1.050 Vel =_11.04 22 38 16.80 122.87 2 X 10.461 34.250 120 53.487 to 0.0 10.461 0.0 23 38 248.63 2.157 0.0 44.711 0.4117 18.408 Vel = 21.83 23 38 0.0 2 T 12.307 2.000 120 71.895 to 0.0 12.307 0.0 24 38 248.63 2.157 0.0 14.307 0.4117 5.890 Vel= 21.83 0.0 24 248.63 77.785 K Factor= 28.19 25 38 -5.75 2 T 12.307 2.000 120 78.923 to 0.0 12.307 0.0 26 38 -5.75 2.157 0.0 14.307 -0.0004 -0.006 Vel = 0.50 26 38 0.0 2 2X 20.921 100.000 120 78.917 to 0.0 20.921 0.0 27 38 -5.75 2.157 0.0 120.921 -0.0004 -0.046 Vel = 0.50 27 38 0.0 2 T 12.307 2.000 120 78.871 to 0.0 12.307 0.0 28 38 -5.75 2.157 0.0 14.307 -0.0004 -0.006 Vel = 0.50 0.0 28 -5.75 78.865 K Facto_r= -0.65 29 38 -3.50 2 T 12.307 2.000 120 79.953 to 0.0 12.307 0.0 30 38 -3.5 2.157 0.0 14.307 -0.0002 -0.003 Vel = 0.31 30 38 0.0 2 2X 20.921 100.000 120 79.950 to 0.0 20.921 0.0 31 38 _ -3.5 2.157 0.0 120.921 -0.0001 -0.018 Vel = 0.31_ 31 38 0.0 2 T 12.307 2.000 120 79.932 to 0.0 12.307 0.0 32 38 -3.5 2.157 0.0 14.307 -0.0001 -0.002 Vel = 0.31 0.0 _32 -3.50 79.930 K Factor=_ -0.39 _ 33 38 -1.95 2 T 12.307 2.000 120 80.919 to 0.0 12.307 0.0 34 38 -1.95 2.157 0.0 14.307 -0.0001 -0.001 Ve_I = 34 38 0.0 2 2X 20.921 100.000 120 80.918 to 0.0 20.921 0.0 35 38 -1.95 2.157 0.0 120.921 0 -0.006 Vel = 0.17 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 9 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes **** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 35 38 0.0 2 T 12.307 2.000 120 80.912 to 0.0 12.307 0.0 36 38 -1.95 2.157 0.0 _14.307 -0.0001 -0.001 Vel= 0.17 0.0 36 -1.95 80.911 K Factor= -0.22 37 38 -0.86 2 T 12.307 2.000 120 81.981 to 0.0 12.307 0.0 38 38 -0.86 2.157 0.0 14.307 0 M Vel= 0.08 _ 38 38 0.0 2 2X 20.921 100.000 120 81.981 to ' 0.0 20.921 0.0 39 38 -0.86 2.157 0.0 120.921 0 -0.001 Vel= 0.08 39 3p 0.0 2 T 12.307 2.000 120 81.980 to 0.0 12.307 0.0 �40, -0.86 2.157 0.0 14.307 -0.0001 -0.001 Vet= 0.08 0.0 40 -0.86 81.979 K Factor= -0.09 _ ---- 41 3 -0.2_5 2 T 12.307 2.000 120 83.046 to 0.0 12.307 0.0 4L -0.25_ G.15 7 0.0 14.307 0 0.0 V%al- 0.02 _ 42 36 2 2X 20.921 100.000 120 83.046 to 0.0 20.921 0.0 43 �­�5 2.157 0.0 120.921 0 0.0 Vel = 0.02 43 0.0 2 T 12.307 2.000 120 83.046 to 0.0 12.307 0.0 44 38 -0.25 2.157 0.0 14.307 0 0.0 Vel= 0.02 0.0 44 -0.25 _ 83.046 Factor= -0.03 45 38 -0.03 2 T 12.307 2.000 120 , 84,111 to 0.0 12.307 0. 46 3F -0.03 2.157 0.0 14_307 0 ( .0 �i = 0 46 a6 0.0 2 2X 20.921 100.000 120 84.111 to 0.0 20.921 0.0 _47 38 -0.03 2.157 0.0 120.921 0 0.0 Vel=0 47 38 0.0 2 T 12.307 2.000 120 84.111 to 0.0 12.307 0.0 48 38 -0.03 2.157 0.0 14.307 0 0.0 Vel=0 0.0 48 -0.03_______.__ 84.111 K Factor= 0 49 38 0.0 2 T 12.307 2.000 120 85.177 to 0.0 12.307 0.0 50 38 0.0 2.157 0.0 14.307 0 0.0 Vel=0 50 38 0.0. 2 2X 20.921 100.000 120 85.177 to 0.0 20.921 0.0 51 38 0.0 2.157 0.0 9 20.921 0 0.0 Vel= 0 51 38 0.0 2 T 12.307 2.000 120 85.177 to 0.0 12.307 0.0 52 38 0.0 2.157 0.0 14.307 0 0.0 Vel=0 _ Computer Programs by Hydratec Inc. Revision: 50,52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 10 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe *****'* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 0.0 52 0.0 85.177 K Factor=0 53 38 0.02 2 T 12.307 2.000 120 86.224 to 0.0 12.307 0.0 54 38 0.02 2.157 0.0 14.307 0 0.0 Vel =0 54 38 0.0 2 2X 20.921 100.000 120 86.224 to 0.0 20.921 0.0 55 38 0.02 2.157 0.0 120.921 0 0.0 Vel =0 55 38 0.0 2 T 12.307 2.000 120 86.224 to 0.0 12.307 0.0 56 38 0.02 2.157 0.0 14.307 0 0.0 Vel = 0 0.0 56 0.02 86.224 K Factor= 0 57 38 - 0.17 2 T 12.307 2.000 120 87.271 to 0.0 12.307 0.0 58 38 0.17 2.157 0.0 14.307 0 0.0 Vel= 0.01 _ 58 38 0.0 2 2X 20.921 100.000 120 87.271 to 0.0 20.921 0.0 _59 38 0.17 2.157 0.0 120.921 0 0.0 Vel = 0.01 _ 59 38 0.0 2 T 12.307 2.000 120 87.271 to 0.0 12.307 0.0 60 38 0.17 2.157 0.0 14.307 0 0.0 Vel= 0.01 0.0 - _60 0.17 87.271 K'Factor= 0.02 61 38 0.66 2 T 12.307 2.000 120 88.318 to 0.0 12.307 0.0 62 38 0.66 2.157 0.0 14.307 0 0.0 Vel = 0.06 62 38 0.0 2 2X 20.921 100.000 120 88.318 to 0.0 20.921 0.0 63 38 0.66 2.157 0.0 _120.921 0 0.0 Vel = 0.06 63 38 0.0 2 T 12.307 2.000 120 88.318 to 0.0 12.307 0.0 64 38 0.66 2.157 0.0 14.307 0.0001 0.001 Vel= 0.06 0.0 64 0.66 88.319 K Factor= 0.07 65 38 1.61 2 T 12.307 2.000 120 89.362 to 0.0 12.307 0.0 66 38 1.61 2.157 0.0 14.307 0.0001 0.001 Vel = 0.14 66 38 0.0 2 2X 20.921 100.000 120 89.363 to 0.0 20.921 0.0 67 38 1.61 2.157 0.0 120.921 0 0.004 Vel = 0.14 67 38 0.0 2 T 12.307 2.000 120 89.367 to 0.0 12.307 0.0 68 38 1.61 2.157 0.0 14.307 0.0001 0.001 Vel = 0.14 0.0 68 1.61 89.368 K Factor= 0.17 69 38 3.10 2 T 12.307 2.000 120 90.403 to 0.0 12.307 0.0 70 38 3.1 2.157 0.0 14.307 0.0001 0.002 Vel = 0.27 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 11 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe """*" Notes **** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 70 38 0.0 2 2X 20.921 100.000 120 90.405 to 0.0 20.921 0.0 71 38 3.1 2.157 0.0 120.921 0.0001 0.015 Vel= 0.27 71 38 0.0 2 T 12.307 2.000 120 90.420 to 0.0 12.307 0.0 72 38 3.1 2.157 0.0 14.307 0.0001 0.002 Vel = 0.27 0.0 72 3.10 90.422 K Factor= 0.33 73 38 5.19 2 T 12.307 2.000 120 91.436 to 0.0 12.307 0.0 74 38 5.19 2.157 0.0 14.307 0.0003 0.004 Vel= 0.46 74 38 0.0 2 2X 20.921 100.000 120 91.440 to 0.0 20.921 0.0 75_.. _ 35_ ,.. _- : . _ ,5..19 2.157 0.0 120.921 0.0003 0.039 Vel = 0.46 75 38 0.0 2 T 12.307 2.000 120 91.479 to 0.0 12.307 0.0 76 38 _ 5.19 2.157 0.0 14.307 0.0003 0.004 Vel= 0.46 0.0 78 C.1 g 91.483 K Factor= 0.54 77 38 7.92 2 T 12.307 2.000 120 92.454 to 0.0 12.307 0.0 78 38 7.92 2.157 0.0 14.307 0.0007 0.010 Vel = 0.70 78 38 0.0 2 2X 20.921 100.000 120 92.464 to 0.0 20.921 0.0 79 38 _ 7.92 2.157 0.0 120.921 0.0007 0.0.85 Vel = 0.70--__ 79 38 0.0 2 T 12.307 2.000 120 92.549 to 0.0 12.307 0.0 80 38 7.92 2.157 0.0 14.307 0.0007 0.010 Vel = 0.70 0.0 80 7.92 _ 92.559 K Factor= 0.82 81 38 11.34 2 T 12.307 2.000 120 93.452 to 0.0 12.307 0.0 82 38 11.34 2.157 0.0 14.307 0.0014 0.020 Vel= 1.00 82 38 0.0 2 2X 20.921 100.000 120 93.472 to 0.0 20.921 0.0 83 38 11.34 2.157 _ 0.0 120.921 0.0014 0.165 - Vel= 1.00 83 38 0.0 2 T 12.307 2.000 120 93.637 to 0.0 12.307 0.0 84 38 11.34 2.157 0.0 14.307 0.0013 0.019 Vel = 1.00 0.0 84 11.34 _ 93.656 K Factor= 1.17 85 38 15.49 2 T 12.307 2.000 120 94.422 to 0.0 12.307 0.0 86 38 15.49 2.157 0.0 14.307 0.0024 0.034 Vel= 1.36 86 38 0.0 2 2X 20.921 100,000 120 94.456 to 0.0 20.921 0.0 87 38 15.49 2.157 0.0 _120.921 _0.0024 0.293 _ Vel = 1.36 i Computer Programs by Hydratec Inc. Revision: 50.52.1 i Final Calculations - Hazen-Williams S. A. COMUNALE Page 12 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 87 38 0.0 2 T 12.307 2.000 120 94.749 to 0.0 12.307 0.0 88 38 15.49 2.157 0.0 14.307 0.0024 0.035 Vel= 1.36 0.0 88 15.49 94.784 K Factor= 1.59 89 38 20.40 2 T 12.307 2.000 120 95.351 to 0.0 12.307 0.0 90 38 20.4 2,157 0.0 14.307 0.0041 0.058 Vel= 1.79 90 38 0.0 2 2X 20.921 100.000 120 95.409 to 0.0 20.921 0.0 91 38 20.4 2.157 0.0 120.921 0.0040 0.488 Vel= 1.79 _ 91 38 0.0 2 T 12.307 2.000 120 95.897 to 0.0 12.307 0.0 92 38 20.4 2.157 0.0 14.307 0.0041 0.058 Val= 1.79 0.0 92 20.40 95.955 K Factor= 2.08 93 38 26.11 2 T 12.307 2.000 120 96.231 to 0.0 12.307 0.0 _94 38 26,11 2.157 0.0 14.307 0.0064 0.091 Vel = 2.29 94 38 0.0 2 2X 20.921 100.000 120 96.322 to 1 0.0 20.921 0.0 95 38 26.11 2.157 0.0 120.921 0.0064 0.770 Val = 2.29 95 38 0.0 2 T 12.307 2.000 120 97.092 to 0.0 12.307 0.0 96 38 26.11 2.157 0,0 14.307 0.0064 0.091 Vel= 2.29 0.0 96 26.11 97.183 K Factor= 2.65 97 38 32.65 2 T 12.307 2.000 120 97.047 to 0.0 12.307 0.0 98 38` 32.65 2.157 0.0 14.307 0.0096 0.138 Vel= 2.87 _ 98 38 0.0 2 2X 20.921 100.000 120 97.185 to 0.0 20.921 0.0 99 38 - 32.65 2.157 0.0 120.921 0.0096 1.164 Vel= 2.87 _ 99 38 0.0 2 T 12,307 2.000 120 98.349 to 0.0 12.307 0.0 100 38 32.65 2.157 0.0 14.307 0.0096 0.137 Vel = 2.87 0.0 - _100__ 32.65 98.486 K Factor= 3.29 _ 101 38 40.03 2 T 12.307 2.000 120 97.788 to 0.0 12.307 0.0 102 38 ` 40.03 2.157 0.0 14.307 0.0140 0.201 Vel = 3.51 102 38 0.0 2 2X 20,921 100.000 120 97.989 to 0.0 20.921 0.0 103 38 _ 40.03 2.157 0.0 _120.921 0.0140 1.698 Vel = 3.51 103 38 0.0 2 T 12.307 2.000 120 99.687 - - --! to 0.0 12.307 0.0 104 , 38_______ 40.03 _2_157 0.0 14.307 0.0140 0.200 Vel= 3.51 0.0 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 13 SYSTEM 1 Date 7.6.18 Node! Elevi K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe **'*'** Notes ***** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 104 40.03 _ 99.887 K Factor= 4.01 _ 105 38 48.36 2 T 12.307 2.000 120 98.447 to 0.0 12.307 0.0 _1 .6 38 48.36 2.157 0.0 14.307 0.0199 0.285 Vel= 4.25_-i 106 38 0.0 2 2X 20.921 100.000 120 98.732 to 0.0 20.921 0.0 107 38 48.36 2.157 0.0 120.921 0.0199 2.408 Vel= 4.25 107 38 0.0 2 T 12.307 2.000 120 101.140 to 0.0 12.307 0.0 108 38 48.36 2.157 0.0 14.307 0.0199 0.285 Vel= 4.25 0.0 108 48.36 101.425 K Factor= 4.80 109 38 57.67 2 T 12.307 2.000 120 99.011 to 0.0 12.307 0.0 110 _ 38 57.67 2.157 0.0 _14.307 0.0276 0.395 Vel 5 06 110 38 - 0.0 2 2X 20.921 100.000 120 99.406 to 0.0 20.921 0.0 111 38 57.67 2.157 0.0 120.921 0.0276 3.334 Vel= 5.06 111 JU 0.0 2 T 12.307 2.000 120 102.1 to 0.0 12.307 0.0 112 38 57.67 2.157 0.0 14.307 0.0276 0.395 Vel= 5.06 - 0.0 112_ _ _ _ 57.67 103,135 K Factor= 5.68 113 38 67.90 2 T 12.307 2.000 120 99.464 to 0.0 12.307 0.0 114 38 67.9 2.157 0.0 14.307 0.0373 0.534 Vel= 5.96 114 38 0.0 2 2X 20.921 100.000 120 99.998 to 0.0 20.921 0.0 115_ 38 67.9 2.157 0.0 120.921 0.0373 4.511 Vel = 5.96 115 38 0.0 2 T 12.307 2.000 120 104.509 to 0.0 12.307 0.0 116 38 67.9 2.157 0.0 14.307 0.0373 0.534 Vel= 5.96 0.0 116 67.90 105.043 K Factor= 6.63 _ 117 38 -- 79.07 2 T 12.307 2.000 120 99.802 to 0.0 12.307 0.0 118 38 79.07 2.157 0.0 14.307 0_0494 0.707 Vel= 6.94 j 118 38 0.0 2 2X 20.921 100.000 120 100.509 to 0.0 20.921 0.0 119_ 38 _ 79.07 2.157 0.0 120.921 0.0495 5.980 Vel= 6.94 119 38 0.0 2 T 12.307 2.000 120 106.489 to 0.0 12.307 0.0 120 38 79.07 2.157 0.0 14.307 0.0494-0.707 Vel= 6.94 0.0 120 _ 79.07 _ 107.196 K Factor= 7.64 _ 121 38 91.21 2 T 12.307 2.000 120 100.024 to 0.0 12.307 0.0 122 38 91.21 2.157 0.0 14.307 0.0644 0.922 Vel= 8.01 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 14 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ***"*** Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 122 38 0.0 2 2X 20.921 100.000 120 100.946 to 0.0 20.921 0.0 123 38 91.21 2.157 0.0 120.921 0.0644 7.786 Vel= 8.01 123 38 0.0 2 T 12.307 2.000 120 108.732 to 0.0 12.307 0.0 124 38 91.21 2.157 0.0 14.307 0.0644 0.922 Vel= 8.01 0.0 i 124 91.21 109.654 K Factor= 8.71 125 38 104.30 2 T 12.307 2.000 120 100.142 to 0.0 12.307 0.0 126 38 104.3 2.157 0.0 14.307 0.0825 1.181 Vel = 9.16 126 38 0.0 2 2X 20.921 100.000 120 101,323 _ to 0.0 20.921 0.0 127 38 104.3 2.157 0.0 120.921 0.0825 9.980 Vel = 9.16 127 38 0.0 2 T 12.307 2.000 120 111,303 to 0.0 12.307 0.0 128 38 104.3 2.157 0.0 14.307 0.0825 1.181 Vel = 9.16 0.0 28 _ 104.30 112.484 K Factor= 9.83 129 38 118.34 2 T 12.307 2.000 120 100.179 to 0.0 12.307 0.0 _130_ 38 118.34 2.157 0.0 14.307 0.1043 1.492 Vel = 10.39 130 38 0.0 2 2X 20.921 100.000 120 101.671 to 0.0 20.921 0.0 131 38 118.34 2.157 0.0 120.921 0.1043 12.607 Vel= 10.39 131 38 0.0 2 T 12.307 2.000 120 114.278 to 0.0 12.307 0.0 132 38 118.34 2.157 0.0 14.307 0.1043 1.492 Vel_= 10.39 0.0 132 118.34 115.770 K Factor= 11.00 1 38 239.37 4 0.0 9.500 120 77298 to 0.0 0.0 0.0 38 239.37 4.26 0.0 9.500 0.0139 0.132 Val = 5.39 9 38 239.56 4 0.0 9.500 120 77.430 to 0.0 0.0 0.0 17 38 478.93 4.26 0.0 9.500 0.0503 0.478 Vel = 10.78 17 38 240.27 4 0.0 9.500 120 77.908 to 0.0 0.0 0.0 -2-5 __ 38 719.2 4.26 0.0 9.500 0.1068 1.015 Vel = 16.19 25 38 5.75 4 0.0 9.500 120 78.923 to 0.0 0.0 0.0 _29 38 724.95 4.26 0.0 9.500 0.1084 1.030 Vel= 16.32 _ 29 38 3.49 4 0.0 8.833 120 79.953 to 0.0 0.0 0.0 33 38 _ 728.44 4.26 0.0 8.833 0.1094 0.966 Vel = 16.40 33 38 1.96 4 0.0 9.667 120 80.919 to 0.0 0.0 0.0 37 38 730.4 4.26 0.0 9.667 0.1099 1.062 Vel = 16.44 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 15 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 37 38 0.85 4 0.0 9.667 120 _ 81.981 to 0.0 0.0 0.0 41 38 731.25 4.26 0.0 9.667 0.1102 1.065 Vel = 16.46 41 38 0.25 4 0.0 9.667 120 83.046 to 0.0 0.0 0.0 45 38 731.5 4.26 0.0 9.667 0.1102 1.065 Vel= 16.47 45 38 0.03 4 0.0 9.667 120 84.111 to 0.0 0.0 0.0 _49 38 731.53 4.26 0.0 9.667 0.1103 1.066 Vel = 16.47 49 38 0.0 4 0.0 9.500 120 85.177 to 0.0 0.0 0.0 53 38 731_53 4.26 0.0 9.500 0.1102 _1.047 Vel= 16.47 _ _ 53 38 '0.01 4 0.0 9.500 120 86.224 0 _,0 0 0 0.0 57 38 731.52 4.26 0.0 9.500 0. 102 1.y047 del= 16.47 57 38 -0.17 4 0.0 9.500 120 87.271 to 0.0 0.0 0.0 61 38 731.35 4.26 0.0 9.500 0.1102 1.047 Vel= 16.46 61 30 -0.66 4 0.0 9.500 120 88.318 to 0.0 0.0 0.0 0.0 9.500 0.1099 1.044 Vel = 16.45 65 38 730.69 4.26 65 38 -1.61 4 0.0 9.500 120 89.362 to 0.0 0.0 0.0 69 38 729.08 4.26 0.0 9.500 0.1096 1.041 Vel= 16.41 69 38 -3.10 4 0.0 9.500 120 90.403 to 0.0 0.0 0.0 73 38 _ 725.98 4.26 0.0 9.500 0.1087 1.033 Vel= 16.34 73 36 -5.18 4 0.0 9.500 120 91.436 to 0.0 0.0 0.0 77 38 720.8 4.26 0.0 9.500 0.1072 1.018 Vel= 16.23 77 38^ -7.92 4 0.0 9.500 120 92.454 to 0.0 0.0 0.0 81 38 712.88 4.26 0.0 9.500_ 0.1051 0.998 Vel = 16.05 81 38 -11.34 4 0.0 9.500 120 93.452 to 0.0 0.0 0.0 85 38 701.54 4.26 0.0 9.500 0.1021 0.970 Vel= 15.79 85 38 --- 15.49 4 0.0 9.500 120 94.422 to 0.0 0.0 0.0 89 38 686.05 4.26 0.0 9 500„ 0.0978 0.929_ Vel= 15.44 89 38 -20.40 4 0.0 9.500 120 95.351 to 0.0 0.0 0.0 - - 0.0 9.500 0.0926 0.880 Vel= 14.98 93 38 665.65 4.26 93 38 -26.12 4 0.0 0.0 9.0 0 120 90.231 to 97 38 639.53 4.26 0.0 9.500 0.0859 0.816 Vel= 14.40 j 97`--38 --- -32.64 4 0.0 9.500 120 97.047 to 0.0 0.0 0.0 101 38 606.89 4.26 0.0 9.500 0.0780 0.741 Vel= 13.66 i i I Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. CQMUNALE Page 16 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng s Pe Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 101 38 -40.03 4 0.0 9.583 120 97.788 to 0.0 0.0 0.0 105 38 566.86 4.26 0.0 9.583 0.0688 0.659 Vel= 12.76 105 38 -48.36 4 0.0 9.667 120 98.447 to 0.0 0.0 0.0 _109 38 518.5 4.26 0.0 9.667 0.0583 0.564 Vel= 11.67 109 38 -57.67 4 0.0 9.667 120 99.011 to 0.0 0.0 0.0 113 38 460.83 4.26 0.0 9.667 0.0469 0.453 Vel = 10.37 113 38 -67.90 4 0.0 9.667 120 99.464 to 0.0 0.0 0.0 117 38 392.93 4.26 0.0 9.667 0.0350 0.338 Vel= 8.84 117 38 -79.08 4 0.0 9.667 120 99.802 to 0.0 0.0 0.0 121 38 313.85 4.26 0.0 9.667 0.0230 0.222 Vel= 7.06 121 38 -91.21 4 0.0 9.667 120 100.024 to 0.0 0.0 0.0 125 38 222.64 4.26 0.0 9.667 0.0122 0.118 Vel= 5.01 125 38 -104.30 4 0.0 9.667 120 100.142 to 0.0 0.0 0.0 _129 38 118.34 4.26 0.0 9.667 0.0038 0.037 Vel= 2.66 0.0 129 118.34 100.179 K Factor= 11.82 8 38 247.50 4 0.0 9.500 120 77.135 to 0.0 0.0 0.0 16 38 247.5 4.26 0.0 9.500 0.0148 0.141 Vel= 5.57 16 38 247.74 4 0.0 9.500 120 77.276 to 0.0 0.0 0.0 24 38 495.24 4.26 0.0 9.500 0.0536 0.509 Vel= 11.15 24 38 248.63 4 0.0 9.500 120 77.785 to 0.0 0.0 0.0 28 38 743.87 4.26 0.0 9.500 0.1137 1.080 Vel = 16.74 28 38 -5.75 4 0.0 9.500 120 78.865 to 0.0 0.0 0.0 32 38 738.12 4.26 0.0 _9.500 0.1121 1.065 Vel = 16.61 32 38 -3.50 4 0.0 8.833 120 79.930 to 0.0 0.0 0.0 _36__ 38_ _ 734.62 4.26 0.0 8.833 _0.111.1 0.981 Vel= 16.54 36 38 -1.95 4 0.0 9.667 120 80.911 to 0.0 0.0 0.0 40 38 732.67 4.26 0.0 9.667 0.1105 1.068 Vel = 16.49 --------38 --------732.67 4.26 --- -- -- --- ---- 40 38 -0.85 4 0.0 9.667 120 81.979 to 0.0 0.0 0.0 44__ 38 _ _ _ 731.82 4.26 0.0 _ 9.667 0.1104 1.067 Vel= 16.47 44 38 -0.25 4 0.0 9.667 120 83.046 to 0.0 0.0 0.0 48 38 731.57 4.26 0.0 9.667 0.1102 1.065 Vel = 16.47 48 38 -0.03 4 0.0 9.667 120 84.111 to 0.0 0.0 0.0 52 38 731.54 4.26 0.0 9.667 0.1103 1.066 Vel = 16.47 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 17 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe %Fact Pt to or Ftng's Pe Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf _.-............ _ 52 38 -0.01 4 0.0 9.500 120 85.177 to 0.0 0.0 0.0 56 38 731.53 4.26 _ 0.0 -9.500 0.1102 1.047 Vel= 16.47 56 38 0.02 4 0.0 9.500 120 86.224 to 0.0 0.0 0.0 60 38 731.55 4.26 0.0 9.500 0.1102 1.047 Vel= 16.47 60 38 0.17 4 0.0 9.500 120 87.271 to 0.0 0.0 0.0 _64 38 731.72 4.26 0.0 9.500 0.1103 1.048 Vel= 16.47 64 38 0.65 4 0.0 9.500 120 88.319 to 0.0 0.0 0.0 68 38 732.37 4.26 0.0 9.500 0.1104 1.049 Vel= 16.49 _ 68 38 1.61 4 0.0 9.500 120 89.368 to 0.0 0.0 0.0 72 38 _733.98 4.26 0.0.. 9 6G(T_ 011[�J 1:0'64' yel- Tt5:52 72 38 3.10 4 0.0 9.500 120 90.422 to 0.0 0.0 0.0 76 38 737.08 4.26 0.0 9.500 0.1117 1.061 Vel= 16.59 76 30 -- -_ 5.19 4 0.0 9.500 120 �91.483 to 0.0 0.0 0.0 80 _ 38 742.27 4.26 0.0 9.500 0.1133 1.076 Vel= 16.71 80 38 7.92 4 0.0 9.500 120 92.559 to 0.0 0.0 0.0 84 _38 750.19 4.26 0.0 9.500 0.1155 1.097 Vel= 16.89 - 84 38 11.34 4 0.0 9.500 120 93.656 to 0.0 0.0 0.0 88 38 761.53 4.26 0.0 9.500 0_1187 1.128 Vel= 17.14 88 38 15.49 4 0.0 9.500 120 94.784 to 0.0 0.0 0.0 92 38 777.02 4.26 0.0 9.500 0.1233 1.171 Vel= 17.49 92 38 20.40 4 0.0 9.500 120 95.955 to 0.0 0.0 0.0 _ 0.0 9.500 0.1293 1.228 Vel= 17.95 96 38 797.42 4.26 96 38 26.11 4 0.0 9.500 120 97.183 to 0.0 0.0 0.0 100 38 823.53 4.26 0.0 9.500 _ 0.1372 1.303 Vel= 18.54 - 100 38 32.65 4 0.0 9.500 120 98.486 to 0.0 0.0 0.0 104 38 856.18__ 4-26 _ _0.0 9.500 0.1475 1.401 Vel= 19.27 104 38 40.03 4 0.0 9.583 120 99.887 to 0.0 0.0 0.0 108 38 896.21 4.26 0.0 9_583 0.1605 1.538 Vel = 20.17 108 38 48.36 4 0.0 9.667 120 101.425 to 0.0 0.0 0.0 112_ 38 _ 944.57 4.26 0.0 9.667 0.1769� 1.710 Vel = 21.26 112 38 57.67 4 0.0 9.667 120 103.135 to 0.0 0.0 0.0 116 38 1002.24 4.26 0.0 9.667 0.1974 1.908 Vel = 22.56 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 18 SYSTEM 1 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 116 38 67.90 4 0.0 9.667 120 105.043 to 0.0 0.0 0.0 12 0 38 10 70.14 4.26 0.0-- 9.667 0.2227 2.153 Vel = 24.09 120 38 79.08 4 0.0 9.667 120 107.196 to 0.0 0.0 0.0 124 38 1149.22 4.26 0.0 9.667 0.2543 2.458 Vel= 25.87 124 38 91.20 4 0.0 9.667 120 109.654 _ to 0.0 0.0 0.0 128 38 1240.42 4.26 0.0 9.667 0.2927 2.830 Vel= 27.92 128 38 104.30 4 0.0 9.667 120 112.484 to 0.0 0.0 0.0 132 38 ^1344.72 4.26 0.0 9.667 0.3399 3.286 Vel = 30.27 132 38 118.35 4 0.0 2.000 120 115.770 to 0.0 0.0 0.0 FMJ 38 1463.07 4.26 0.0 2.000 0.3975 0.795 Vel = 32.93 0.0 __FMJ 1463.07 116.565 K Factor= 135.51 FMJ 38 1463.07 6 2V 25.147 221.250 120 116.565 to 0.0 25.147 0.0 TR1 38 1463.07 6.357 0.0 246.397 0.0566 13.937 Vel= 14.79 TR1 38 0.0 6 T 37.72 37.000 120 130.502 to 0.0 37.720 16.592 * Fixed Loss= 1 BR1 2 1463.07 6.357 0.0 74.720 0.0566 4.227 Vel= 14.79 BR1 2 1­1100 100.00 8 T 41.108 4.000 120 151.321 to 0.0 41.108 0.0 Ll 2 1563.07 8.249 0.0 45.108 0.0180 0.810 Vel = 9.38 Ll 2 0.0 12 5L 99.669 830.000 15.0 152.131 to F 14.397 120.710 0.0 UG 2 1563.07 11.2 G 6.645 950.710 0.0027 2.551 Vel = 5.09 UG 2 H150 150.00 10 S 61.525 15.000 150 154.682 to B 21.254 100.677 Q.0 PO 2 1713.07 9.42 L 17.898 115.677 0.0074 0.854 Vel = 7.89 0.0 PO 1713.07 155.536 K Factor= 137.36 Computer Programs by Hydratec Inc. Revision: 50.52.1 AutoPeaking Summary S.A. COMUNALE rage 19 SYSTEM 1 Date 7.6.18 Auto Peaking Summary- List of Pipes for Area Calculated Left Right Side Side From To Length From To Length 2 3 38.750 6 7 34.250 10 11 38.750 14 15 34.250 18 19 38.750 22 23 34.250 Flow Safety Pressure Required Margin Differential Left 9.000 1 1713.213 9.434 -0.144 Area Calculated 1 1713.068 9.291 0.000 Right 9.000 1 1713.484 9.722 -0.432 Typical Distance Between Heads = 9.000 Split Point Used in Worst Area Peaked = 4 `1 i { i Computer Programs by Hydratec Inc. Revision: 50.52.1 S.A. COMUNALE Page 1 SYSTEM 2 Date 7.6.18 Hydraulic Desian Information Sheet Tdame - ALDI'S SOUTH WINDSOR DRY EXPANSION Fate - 7.6.18 Location - 295 RYE ST, SOUTH WINDSOR, CT, 06074 Building - System No. - 2 Contractor - S. A. CPOMUNALE Contract No. - 58056-018 Calculated By - A SMITH Drawing No. - 4 OF 5 Construction: ( ) Combustible (X) Non-Combustible Ceiling Height - 391-0" Occupancy - HIGH -PILED STORAGE S (X) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. •Y ) Figure Curve S Other HIGH-PILED STORAGE T Specific Ruling Made By Date E -- M Number of ESFR Sprinklers - 12 System Type Sprinkler/Nozzle End Head Pressure (PSI) - 52 (X) Wet Make RELAIBLE D ESFR K-Factor - 16.8 ( ) Dry model JL-17 Elevation at Highest Outlet - 38`-0" ( ) Deluge Size %" S dose Allowance - Inside - 100 ( ) Preaction K-Factor 16.8 I Rack Sprinkler Allowance - { } Other Temp.Rat.165° G Hose Allowance - Outside - 150 N Note Calculation Flow Required - 1712.7 Press Required - 153.2 AT PUMP DISCHARGE Summary C-Factor Used: 120 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - Cap. - T Time of Test - Rated Cap.- 2000 Elev.- E Static Press - a Press - 160 R Residual Press - Elev. - 2 Well Flow - Proof Flow S Elevation - TJ P Location - NEW PUMP AND 250,000 GALLON WATER STORAGE TANK P L Source of Information - v C Commodity GROUP A U.E.P. Class I-IV Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled Palletized Rack M --- — { ) Sinale Row ( ) Conven. Pallet —( ) Auto. Storage ( ) Encap. S R ( ) Double Row ( ) Slave Pallet ` ) Solid Shelf ( ) Non :i A ( ) Muit. Row ( ) Open Shelf OC --- -- - R K Flue Spacing learance:Storage to Ceiling A Longitudinal Transverse Horizontal Barriers Provided: �ti��'J, _ J 0 27160 Water Supply Curve C S. A. COMUNALE Page 2 SYSTEM 2 Date 7.6.18 Pump Data: Demand: P1 -Pump Churn Pressure 177 D1 - Elevation 15.592 P2 - Pump Rated Pressure 160 D2-System Flow : 1462.67 P2-Pump Rated Flow 2000 D2-System Pressure : 153.247 P3 - Pump Pressure @ Max Flow 120 Hose ( Demand ) : 250 P3 - Pump Max Flow 3750 D3 - System Demand : 1712.67 Safety Margin 11.586 180 — — 168 P2 156 p 144 D3 R 132 P3 E 120 S 108 S 96 U 8`t R 72 E 60 48 36 24 12 400 800 1200 1600 2000 2400 2800 3200 3600 FLOW( N " 1.85 ) Computer Programs bar Hvdratec Inc. Revisian; '!5(' 92.1 Fittings Used Summary S. A. COMUNALE Page 3 SYSTEM 2 Date 7.6.18 Fitting Legend Abbrev. Name 'h '/ 1 1'/a 1'/2 2 2'/2 3 3'/z 4 5 6 8 10 12 14 16 18 20 24 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 F NFPA 13 45'Elbow 1 1 1 1 2 2 3 3 3 4 5 7 9 11 13 17 19 21 24 28 G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 L NFPA 13 Long Turn Elbow 0.5 1 2 2 2 3 4 5 5 6 8 9 13 16 18 24 27 30 34 40 S NFPA 13 Swing Check 0 0 5 7 9 11 14 16 19 22 27 32 45 55 65 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 V 90'Ell Firelock#001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 4.5 5.1 0 0 0 0 0 X 90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 21 25 33 9.3 11 0 0 0 0 0 Unit Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *. The fittings marked with a *show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a*will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Revision: 50.52.1 Pressure / Flow Summary - STANDARD S. A. COMUNALE Page 4 SYSTEM 2 Date 7.6.18 n_ �i..,., n......'i,. Aron Node Elevation K-Fact Pt n n How ucnoilr No. Actual Actual Reg. 1 38.0 86.04 na 2 38.0 80.53 na 3 38.0 16.8 52.93 na 122.22 0.2 81 52.0 4 38.0 16.8 52.0 na 121.15 0.2 81 52.0 5 38.0 16.8 52.0 na 121.15 0.2 81 52.0 6 38.0 16.8 53.04 na 122.35 0.2 81 52.0 7 38.0 94.64 na 9 38.0 86.17 na 10 38.0 80.65 na 11 38.0 16.8 53.01 na 122.31 0.2 81 52.0 12 38.0 16.8 52.08 na 121.24 0.2 81 52.0 13 38.0 16.8 52.08 na 121.24 0.2 81 52.0 14 38.0 16.8 53.12 na 122.44 0.2 81 52.0 15 38.0 94.77 na 17 38.0 86.65 na 18 38.0 81.1 na 19 38.0 16.8 53.3 na 122.65 0.2 81 52.0 20 38.0 16.8 52.37 na 121.57 0.2 81 52.0 21 38.0 16.8 52.37 na 121.57 0.2 81 52.0 22 38.0 16.8 53.41 na 122.78 0.2 81 52.0 23 38.0 95.25 na 26 38.0 88.57 na 27 38.0 101.28 na 29 38.0 88.46 na 30 38.0 89.4 na 31 38.0 102.58 na 33 38.0 89.01 na 34 38.0 90.01 na 35 38.0 104.02 na 37 38.0 89.43 na 38 38.0 90.53 na 39 38.0 105.9 na 41 38.0 89.7 na 42 38.0 90.92 na 43 38.0 108.11 na 45 38.0 89.83 na 46 38.0 91.22 na 47 38.0 110.72 na 49 38.0 89.87 na 50 38.0 91.46 na 51 38.0 113.78 na 8 38.0 100.46 na 16 38.0 100.6 na 24 38.0 101.11 na 28 38.0 102.19 na 32 38.0 103.52 na 36 38.0 105.02 na 40 38.0 106.99 na 44 38.0 109.33 na 48 38.0 112.1 na 52 38.0 115.37 na FMJ 38.0 116.56 na TR2 38.0 129.01 na BR2 2.0 149.83 na 100.0 LI 2.0 149.84 na UG 2.0 152.39 na 150.0 PO 2.0 153.25 na The maximum velocity is 32.92 and it occurs in the pipe between nodes 52 and FMJ Computer Programs by Hydratec Inc. Revision: 50.52.1 EOD S.A. COMUNALE Page 5 SYSTEM 2 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 1 38 -239.76 2 T 12.307 2.000 120 86.038 to 0.0 12.307 0.0 2 38 -239.76 2.157 0.0 14.307 -0,3850 -5.508 Vel= 21.05 '2 38 0.0 2 X 10.461 61.250 120 80.530 to 0.0 10.461 0.0 3 38 -239.76 2.157 0.0 71.711 -0.3849 -27.603 Vel = 21.05 3 38 16.80 122.22 2 0.0 9.000 120 52.927 to 0.0 0.0 0.0 4 38 -117.54 2.157 0.0 9.000 -0.1030_-0.927 Vel=_10.32 4 38 16.80 121.15 2 0.0 9.000 120 52.000 to 0.0 0.0 0.0 5 38 3.61 2.157 0.0 9.000 0.0002 0.002 Vel= 0.32 _ 5 38 16.80 121.15 2 0.0 9.000 120 52.002 to 0.0 0.0 0.0 6 38 124.76 2.157 0.0 9.000 0.1149 1.034 Vel = 10.95 _ 6 38 16.80 122.34 2 X 10.461 91.750 120 53.036 to 0.0 10.461 0.0 _7 38 247.1 2.157 0.0 102.211 0.4070 41.604 Vel= 21.70 7 38 0.0 2 T 12.307 2.000 120 94.640 to 0.0 12.307 0.0 8 38 247.1 2.157 0.0 14.307 0.4070 5.823 Vel = 21.70 0.0 8 247.10 100.463 K Factor= 24._65 9 38 -239.96 2 T 12.307 2.000 120 86,171 to 0.0 12.307 0.0 10 38 -239.96 2.157 0.0 14.307 -0.3855 -5.516 Vel = 21.07 10 38 0.0 2 X 10.461 61.250 120 80.655 to 0.0 10.461 0.0 11 38 -239.96 2.157 0.0 71.711 -0.3855 -27.647 Vel = 21.07 11 38 16.80 122.31 2 0.0 9.000 120 53.008 to 0.0 0.0 0.0 12 38 -117.65 2.157 0.0 9.000 -0.1031 -0.928 Vel 10.33 _ 12 38 16.80 121.24 2 0.0 9.000 120u 52.080 -_ J to 0.0 0.0 0.0 13 38 3.59 2.157 0.0 9.000 0.0001 0.001 Vel = 0.32 13 38 16.80 121.24 2 0.0 9.000 120 52.081 to 0.0 0.0 0.0 1_4_ 38 _ 124.83 2.157 0.0 _9.0_0_0 0.1151 1.036 Vel = 10_.96 14 38 -16.80 122.44 2 X 10.461 91.750 120 53.117 to 0.0 10.461 0.0 15 38 _ 247.27 2.157 _ 0.0 102.211 0.4075 41.656 _Vel = 21.7.1__ _ 15 38 _ 0.0 2 T 12.307 2.000 120 94.773 to 0.0 12.307 0.0 16 38 247.27 1157 0.0 14.307 0.4076 5.831 Vel = 21.71 0.0 16 247.27 100.604 K Factor= 24.65 - -- - ------------ ----..�--- ------------------ ---- -------- ---- _---- 17 38 -240.69 2 T 12.307 2.000 120 86.650 to 0.0 12.307 0.0 18 38 -240.69 2.157 0.0 14.307 -0.3877 -5.547 Vel = 21.13 Computer Programs by Nydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 6 SYSTEM 2 Date 7.6.18 Node! Eiev-i K Qa Nom FiUing Pipe CFact Pt to or Ftng's Pe Notes * **= Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 18 38 0.0 2 X 10.461 61.250 120 81.103 to 0.0 10.461 0.0 19 38 -240.69 2.157 _0_.0 7.1.711 -0.3877 -27.803 Vel = 21.13 19 38 16.80 -122.65 2 0.0 9.000 120 53.300 to 0.0 0.0 0.0 20_ 38 -118.04 2.157 _ 0.0 9.000 -0.1038 -0.934 Vel = 10.36 20 38 16.80 121.57 2 0.0 9.000 120 52.366 to 0.0 0.0 0.0 21 38 3.53 2.157 _ 0.0 9.000 0.0002 0.002 Vel = 0.31 _ 21 38 16.80 121.58 2 0.0 9.000 120 52.368 to 0.0 0.0 0.0 _22 38 125.11 2.157 0.0 9.000 0.1156 1.040 Vel= 10.98 22 38 16.80 122.77 2 X 10.461 91.750 120 53.408 to 0.0 10.461 0.0 23 38. . . 247.88 IJ57 .. ........ . .O:b TfT2 2-11_._. "0:4094 4T:846'.... ., f= 2'1":16 ._.-.. 23 38 0.0 2 T 12.307 2.000 120 95.254 to 0.0 12.307 0.0 24 38 247.88 2.157 0.0 14.307 0.4094 5.857 Vel= 21.76 0.0 24 _2.47.88 101.111 K Factor= 24.65 25 38 90.33 2 T 12.307 2.000 120 87.668 to 0.0 12.307 0.0 26 38 90.33 2.157 0,0 14.307 0.0633 0.905 Vel = 7.93 ---- _ T ........__ ----- 26 38 0.0 2 2X 20.921 180.000 120 88.573 to 0.0 20.921 0.0 27 38 90.33 2.157 0.0 200.921 0.0633 12.709 Vel= 7.93 27 38 0.0 2 T 12.307 2.000 120 101.282 to 0.0 12.307 0.0 28 38 90.33 2.157 0.0 14.307 0.0633 0.905 Vel= 7.93 0.0 _28 90.33 102.187 K Factor= 8.94 29 38 92.11 2 T 12.307 2.000 120 88.463 to 0.0 12.307 0.0 30 38 92.11 2.157 0.0 _14.307 0.0656 0.938 Vel = 8.09 _ 30 38 0.0 2 2X 20.921 180.000 120 89.401 to 0.0 20.921 0.0 31 38 92.11 2.157 0.0 200.921 0.0656 13.178 Vel = 8.09 31 38 0.0 2 T 12.307 2.000 120 102.579 to 0.0 12.307 0.0 32 38 92.11 2.157 0.0 14.307 0.0656 0.938 Vel= 8.09 0.0 32 _ 92.11 _ 103.517 K Factor= 9.05 33 38 95.21 2 T 12.307 2.000 120 89.014 to 0.0 12.307 0.0 34 38 95.21 2.157 0.0 14.307 0.069.8 0.998 Vel_= 8.36 34 38 0.0 2 2X 20.921 180.000 120 90.012 to 0.0 20.921 0.0 35 38 95.21 2.157 0.0 200.921 0.0697 14.009 Vel = 8.36 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S.A. COMUNALE Page 7 SYSTEM 2 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ***"*** Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 35 38 0.0 2 T 12.307 2.000 120 104.021 to 0.0 12.307 0.0 36 38 95.21 2.157 0.0 14.307 0.0698 0.998 Vel = 8.36 0.0 36 95.21 105.019 K Factor= 9.29 37 38 100.09 2 T 12.307 2.000 120 89.435 to 0.0 12.307 0.0 38 38 100.09 2.157 0.0 14.307 0.0765 1.094 Vel = 8.79 _ 38 38 0.0 2 2X 20.921 180.000 120 90.529 to 0.0 20.921 0.0 39 38 100.09 2.157 0.0 200.921 0.0765 15.366 Vel = 8.79 39 38 0.0 2 T 12.307 2.000 120 105.895 to 0.0 12.307 0.0 40 38 100.09 2.157 0.0 14.307 0.0765 1.094 Vel = 8.79 0.0 40 100.09 106.989 K Factor= 9.68_ 41 38 106.34 2 T 12.307 2.000 120 89.697 to 0.0 12.307 0.0 42 38 106.34 2.157 0.0 14.307 0.0856 1.224 Vel = 9.34 42 38 0.0 2 2X 20.921 180.000 120 90.921 to 0.0 20.921 0.0 43 38 106.34 2.157 0.0 200.921 0.0855 17.187 Vel = 9.34 43 38 0.0 2 T 12.307 2.000 120 108.108 to 0.0 12.307 0.0 44 38 106.34 2.157 0.0 14.307 0.0856 1.224 Vel = 9.34 0.0 44 106.34 109.332 K Factor= 10.17 _ 45 38 113.84 2 T 12.307 2.000 120 89.828 to 0.0 12.307 0.0 46 38 113.84 2.157 0.0 14.307 0.0971 1.389 Vel = 10.00 _ 46 38 0.0 2 2X 20.921 180.000 120 91.217 to 0.0 20.921 0.0 47 38 113.84 2.157 0.0 200.921 0.0970 19.498 Vel = 10.00 47 38 0.0 2 T 12.307 2.000 120 110.715 to 0.0 12.307 0.0 48 38 113.84 2.157 0.0 14.307 0.0970 1.388 Vel = 10.00 0.0 48 _ 113.84 112.103 K Factor= 10.75 49 38 122.48 2 T 12.307 2.000 120 89.868 to 0.0 12.307 0.0 50 38 122.48 2.157 0.0 14.307 0.1111 1.589 Vel= 10.75 50'- 38 _---'- 0.0 2 2X 20.921 180.000 120 91.457 to 0.0 20.921 0.0 51 38 _ 12.2.48 2.157_ 0.0 200.921 0.1111 22.323__V_eI = 51 38 0.0 2 T 12.307 2.000 120 113.780 to 0.0 12.307 0.0 52 38 122.48 2.157 0.0 14.307 0.1111 1.589 Vel = 10.75 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 8 SYSTEM 2 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pi to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 0.0 52 122.48 115.369 K Factor= 11.40 1 38 239.76 4 0.0 9.500 120 86.038 to 0.0 0.0 0.0 9 38 239.76 4.26 0.0 9.500 0.0140 0.133 Vel = 5.40 9 38 239.96 4 0.0 9.500 120 86.171 to 0.0 0.0 0.0 17 38 479.72 4.26 0.0 9.500 0.0504 0.479 Vel = 10.80 17 38 240.69 4 0.0 9.500 120 86.650 to 0.0 0.0 0.0 25 38 720.41 4.26 0.0 9.500 0.1072 1.018 Vel= 16.22 25 38 -90.33 4 0.0 9.500 120 87.668 to 0.0 0.0 0.0 29 38 630.08 4.26 0.0 9.500 0.0837 0.795 Vel= 14.18 29 38 -92.11 4 0.0 8.833... 120' to 0.0 0.0 0.0 33 38 537.97 4.26 0.0 8.833 0.0624 0.551 Vel = 12.11 33 _ 38 -95.22 4 0.0 9.667 120 89.014 to 0.0 0.0 0.0 37 38 442.75 4.26 0.0 9.667 0.0436 0.421 Vel= 9.97 - 37 38 -100.09 4 0.0 9.667 120 89.435 to 0.0 0.0 0.0 41 38 342.66 4.26 0.0 9.667 0.0271 0.262 Vel= 7.71 41 38 -106.34 4 0.0 9.667 120 89.697 to 0.0 0.0 0.0 45 38 236.32 4.26 0.0 9.667 0.0136 0.131 _Vel= 5.32 45 38 -113.84 4 0.0 9.667 120 89.828 to 0.0 0.0 0.0 49 38 122.48 4.26 0.0 9.667 0.0041 0.040 Vel = 2.76 0.0 49 122.48 89.868 K Factor= 12.92 8 38 ! i247.10 4 0.0 9.500 120 100.463 to 0.0 0.0 0.0 16 38 247.1 4.26 0.0 9.500 0.0148 0.141 Vel= 5.56 16 38 247.28 4 0.0 9.500 120 100.604 to 0.0 0.0 0.0 24 38 494.38 4.26 0.0 9.500 0.0534 0.507 Vel= 11.13 24 38 247.88 4 0.0 9.500 120 101.111 to 0.0 0.0 0.0 28 38 742.26 4.26 0.0 9.500 0.1133 1.076 Vel= 16.71 _ 28 38 90.33 4 0.0 9.500 120 102.187 to 0.0 0.0 0.0 32 38 _ 832.59 4.26_ 0.0 9.500 0.1400 1.330_ Vel= 18.74 32 38 92.11 4 0.0 8.833 120 103.517 to 0.0 0.0 0.0 36 38 924.7 4.26 0.0 8.833 0.1700 1.502 Vel= 20.81 ---- ------..-.--...... _ - _.-.---._ _...- 36 38 95.22 4 0.0 9.667 120 105.019 to 0.0 0.0 0.0 40 38 1019.92 4.26 0.0 9.667 0.2038 1.970 Vel= 22.96 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 9 SYSTEM 2 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 40 38 100.09 4 0.0 9.667 120 106.989 to 0.0 0.0 0.0 44 38 1120.01 4.26 0.0 9.667 0.2424 2.343 Vel = 25.21 44 38 106.34 4 0.0 9.667 120 109.332 to 0.0 0.0 0.0 48 38 1226.35 4.26 0.0 9.667 0.2866 2.771 Vel= 27.60 48 38 113.84 4 0.0 9.667 120 112.103 to 0.0 0.0 0.0 52 38 1340.19 4.26 0.0 9.667 0.3379 3.266 Vel= 30.17 52 38 122.48 4 0.0 3.000 120 115.369 to 0.0 0.0 0.0 FMJ 38 1462.67 4.26 0.0 3.000 0.3973 1.192 Vel = 32.92 0.0 FMJ 1462.67 116.561 K Factor= 135.48 _ FMJ 38 1462.67 6 5V 62.867 157.333 120 116.561 to 0.0 62.867 0.0 TR2 38 1462.67 6.357 0.0 220.200 0.0565 12.449 Vel = 14.79 _ TR2 38 0.0 6 T 37.72 37.000 120 129.010 to 0.0 37.720 16.592 * Fixed Loss= 1 BR2 2 1462.67 6.357 0.0 74.720 0.0565 4.224 Vel= 14.79 BR2 2 1­1100 100.00 8 0.0 1.000 120 149.826 to 0.0 0.0 0.0 LI 2 1562.67 8.249 0.0 1.000 0.0180 0.018 Vel = 9.38 LI 2 0.0 12 5L 99.669 830.000 150 149.844 to F 14.397 120.710 0.0 UG 2 1562.67 11.2 G 6.645 950.710 0.0027 2.549 Vel = 5.09 UG 2 H150 150.00 10 S 61.525 15.000 150 152.393 to B 21.254 100.677 0.0 PO 2 - 1712.67 9.42 L 17.898 115.677 0.0074 0.854 Vel = 7.88 0.0 _Po _ _. 1712.67 ' 153.247 K Factor= 138.35 Computer Programs by Hydratec Inc. Revision: 50.52.1 AutoPeaking Summary S. A. COMUNALE Page 10 SYSTEM 2 Date 7.6.18 Auto Peaking Summary- List of Pipes for Area Calculated Left Right Side Side From To Length From To Length 2 3 61.250 6 7 91.750 10 11 61.250 14 15 91.750 18 19 61.250 22 23 91.750 Flow Safety Pressure l Required Margin Differential Left 9.000 I 1712.733 11.603 -0.017 Area Calculated I 1712.672 11.586 0.000 Right 9.000 1712.785 11.898 -0.313 Typical Distance Between Heads = 9.000 Split Point Used in Worst Area Peaked = 4 i 'j i 1 l 'f Computer Programs by Hydratec Inc. Revision: 50.52.1 j S.A. COMUNALE Page 1 SYSTEM 3 Date 7.6.18 Hvdraulic Desian information Sheet Name - ALDI`S SOUTH WINDSOR DRY EXPANSION Date - 7. 6. 18 Location - 295 RYE ST, SOUTH WINDSOR, CT, 06074 Building - System No. - 3 Contractor - S. A. CPOMUNALE Contract No. - 58056-018 Calculated By - A SMITH Drawing No. - 5 OF 5 Construction: ( ) Combustible (X) Non-Combustible Ceiling Height - 39'-0" Occupancy - HIGH -PILED STORAGE S (X) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y ( ) Figure Curve S Other HIGH-PILED STORAGE T Specific Ruling Made By Date E _ M Number of ESFR Sprinklers - 12 System Type Sprinkler/Nozzle End Head Pressure (PSI) - 52 (X) Wet Make RELAIBLE D ESFR K-Factor - 16.8 ( ) Dry Model JL-17 E Elevation at Highest Outlet - 38'-0" ( ) Deluge Size 3j" S Hose Allowance - Inside - 100 ( ) Preaction K-Factor 16.8 I Rack Sprinkler Allowance - ( } Other Temp.Rat.1650 G Hose Allowance - Outside - 150 N Note Calculation Flow Required - 1712.7 Press Required - 152.4 AT PUMP DISCHARGE Summary C-Factor Used: 120 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - Cap. - T Time of Test - Rated Cap.- 2000 Elev.- E Static Press - @ Press - 160 R Residual Press - Elev. - 2 Well Flow - Proof Flow S Elevation - rJ P Location - NEW PUMP AND 250,000 GALLON WATER STORAGE TANK P L Source of Information - Y C Commodity GROUP A U.E.P. Class I-IV Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled s Palletized Rack M ( ) Single Row ( } Conven. Pallet ( ) Auto. Storage ( ) Encap. S R ( ) Double Row { ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( ) Mutt. Row ( ) Open Shelf O C R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse E Horizontal Barriers Provided: ='c''• NO. 271 .4 __ _ _ _ _ _ _ �� i Water Supply Curve C S. A. COMUNALE Page 2 SYSTEM 3 Date 7.6.18 Pump Data: Demand: P1 - Pump Churn Pressure 177 D1 - Elevation 15.592 P2 -Pump Rated Pressure 160 D2 -System Flow : 1462.67 P2 - Pump Rated Flow 2000 D2 -System Pressure : 152.388 P3 - Pump Pressure @ Max Flow 120 Hose ( Demand ) : 250 P3- Pump Max Flow 3750 D3-System Demand : 1712.67 Safety Margin 12.444 180 Pi 168 P2 156 12 P 144 D3 R 132 E 120 P3 S 108 S 96 U 84 R 72 E 60 48 36 24 12 400 800 1200 1600 2000 2400 2800 3200 3600 FLOW ( NA1.85 ) Computer Programs by Hydrater,Inc, Revision: 50.52 1 Fittings Used Summary S. A. COMUNALE Page 3 SYSTEM 3 Date 7.6.18 Fitting Legend Abbrev. Name '/2 3/4 1 1'/4 1'/2 2 2'% 3 3'/2 4 15 6 8 10 12 14 16 18 20 24 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 0 10 12 19 21 0 0 0 0 0 F NFPA 13 45'Elbow 1 1 1 1 2 2 3 3 3 4 i5 7 9 11 13 17 19 21 24 28 G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 ;2 3 4 5 6 7 8 10 1'I 13 L NFPA 13 Long Turn Elbow 0.5 1 2 2 2 3 4 5 5 6 18 9 13 16 18 24 27 30 34 40 S NFPA 13 Swing Check 0 0 5 7 9 11 14 16 19 22 ,27 32 45 55 65 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 V 90'Ell Firelock#001 0 0 0 0 0 3.5 4.3 5 0 6.8 j8.5 10 13 4.5 5.1 0 0 0 0 0 X 90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 ;21 25 33 9.3 11 0 0 0 0 0 Unit Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *. The fittings marked with a*show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a*will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. (7mmPtitPr Prnyr,:s `lydrnter_. P,vi5ion-'5 1 Pressure / Flow Summary- STANDARD S.A. COMUNALE Page 4 SYSTEM 3 Date 7.6.18 Node Elevation K-Fact Pt Pn Flow Density Area Press No.------- Actual _ Actual Reg_ 1 38.0 91.72 na 2 38.0 85.89 na 3 38.0 16.8 53.04 na 122.35 0.2 81 52.0 4 38.0 16.8 52.0 na 121.15 0.2 81 52.0 5 38.0 16.8 52.0 na 121.15 0.2 81 52.0 6 38.0 16.8 52.93 na 122.22 0.2 81 52.0 7 38.0 88.8 na 9 38.0 91.86 na 10 38.0 86.02 na 11 38.0 16.8 53.12 na 122.44 0.2 81 52.0 12 38.0 16.8 52.08 na 121.24 0.2 81 52.0 13 38.0 16.8 52.08 na 121.24 0.2 81 52.0 14 38.0 16.8 53.01 na 122.31 0.2 81 52.0 15 38.0 88.93 na 17 38.0 92.36 na 18 38.0 86.5 na 19 38.0 16.8 53.41 na 122.78 0.2 81 52.0 20 38.0 16.8 52.37 na 121.57 0.2 81 52.0 21 38.0 16.8 52.37 na 121.57 0.2 81 52.0 22 38.0 16.8 53.3 na 122.65 0.2 81 52.0 23 38.0 89.38 na 25 38.0 93.44 na 26 38.0 93.6 na 27 38.0 95.78 na 29 38.0 94.43 na 30 38.0 94.59 na 31 38.0 96.88 na 33 38.0 95.26 na 34 38.0 95.44 na 35 38.0 97.99 na 37 38.0 96.07 na 38 38.0 96.29 na 39 38.0 99.3 na 41 38.0 96.8 na 42 38.0 97.06 na 43 38.0 100.72 na 45 38.0 97.42 na 46 38.0 97.74 na 47 38.0 102.28 na 49 38.0 97.93 na 50 38.0 98.34 na 51 38.0 103.99 na 53 38.0 98.34 na 54 38.0 98.84 na 55 38.0 105.85 na 57 38.0 98.63 na 58 38.0 99.25 na 59 38.0 107.93 na 61 38.0 98.83 na 62 38.0 99.59 na 63 38.0 110.26 na 65 38.0 98.94 na 66 38.0 99.87 na 67 38.0 112.91 na 69 38.0 98.98 na 70 38.0 100.59 na 71 38.0 123.24 na 8 38.0 94.31 na 16 38.0 94.44 na 24 38.0 94.92 na 28 38.0 95.94 na 32 38.0 97.05 na Computer Programs by Hydratec Inc. Revision: 50.52.1 Flow Summary - Standard S. A. COMUNALE Page 5 SYSTEM 3 Date 7.6.18 ,Node Elevation K-Fact Pt Pn i iovi vanSlt; Area Press No. Actual Actual Reg. _ 36 38.0 98.17 na 40 38.0 99.52 na 44 38.0 100.98 na 48 38.0 102.6 na 52 38.0 104.39 na 56 38.0 106.35 na 60 38.0 108.55 na 64 38.0 111.02 na 68 38.0 113.84 na FMJ 38.0 124.97 na TR3 38.0 127.4 na BR3 2.0 148.21 na 100.0 LI 2.0 148.99 na UG 2.0 151.54 na 150.0 PO 2.0 152.39 na T. -- - _ __:. . _ .4,&p,p hGr.,00n nodes..68-.and-FMJ me maximiu-r-ve�Ucny �a ov7-rvai�u �[vccl�i� �ii cncN,Ncvc r.- Computer Programs by Hydratec Inc. Revision: 50.52.1 EOD S.A. COMUNALE Page 6 SYSTEM 3 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 1 38 -247.12 2 T 12.307 2.000 120 91.717 to 0.0 12.307 0.0 2 38 -247.12 2.157 0.0 14.307 -0.4071 -5.824 Vel = 21.70 2 38 0.0 2 X 10.461 70.250 120 85.893 to 0.0 10.461 0.0 3 38 -247.12 2.157 _ 0.0 80.711 -0.4071 -32.857 Vel = 21.70 3 38 16.80 122.35 2 0.0 9.000 120 53.036 to 0.0 0.0 0.0 4 38 -124.77 2.157 10 9.000 -0.1149 -1.034 Vel= 10.95 _ 4 38 16.80 121.15 2 0.0 9.000 120 52.002 to 0.0 0.0 0.0 5 38 -3.62 2.157 0.0 9.000 -0.0002 -0.002 Vel= 0.32 5 38 16.80 121.14 2 0.0 9.000 120` 52.000 to 0.0 0.0 0.0 --6 38_ 117.52 2.157 0.0 9.000 0.1029 0.926 Vel= 10.3_2_ 6 38 16.80 122.22 2 X 10.461 82.750 120 52.926 to 0.0 10.461 0.0 7 38 239.74 2.157 0.0 93.211 0.3849 35.876 Vel = 21.05 7 38 0.0 2 T 12.307 2.000 120 88.802 to 0.0 12.307 0.0 8 38 239.74 2.157 0.0 14.307 0.3848 5.506 Vel = 21.05 0.0 8 239.74 _ 94.308 K Factor= 24.69 9 38 -247.33 2 T 12.307 2.000 120 91.857 to 0.0 12.307 0.0 10 38 -247.33 2.157 0.0 14.307 -0.4077 -5.833 Vel = 21.72 10 38 0.0 2 X 10.461 70.250 120 86.024 to 0.0 10.461 0.0 11 38 -247.33 2.157 0.0 80.711 -0.4077 -32.907 Vel= 21.72 11 38 16.80 122.44 2 0.0 9.000 120 53.117 to 0.0 0.0 0.0 12 38 -124.89 2.157 0.0 9.000 -0.1151 -1.036 Vel= 10.97 12 38 16.80 121.24 2 0.0 9.000 120 52.081 to 0.0 0.0 0.0 _13 38 -3.65 2.15.7 0.0 _9.000 -0.0002 -0.002 Vel= 0.32 13 38 16.80 121.24 2 0.0 9,000 120 52.079 - to 0.0 0.0 0.0 14 38 117.59 2.157 0.0 _9.000 0.1031 0.928 Vel = 10.32 14 38� 16.80 122.32 2 X 10.461 82.750 120 53.007 to 0.0 10.461 0.0 15 38 239.91 2.157 0.0 93.211 0.385_4_ _35.921 Vel_= 21.06_ _ 15 38 0.0 2 T 12.307 2.000` 120 88.928 v to 0.0 12.307 0.0 16 38 239.91 2.157 0.0 14.307 0.3853 5.513 Vel= 21.06 0.0 16 239.91 94.441 K Factor= 24.69 17 38 -248.07 2 T 12.307 2.000 120 92.365 to 0.0 12.307 0.0 18 38 -248.07 2.157 0.0 14.307 0.4100 -5.866 Vel= 21.78 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 7 SYSTEM 3 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFaCt Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 18 38 0.0 2 X 10.461 70.250 120 86.499 to 0.0 10.461 0.0 19 38 _ -248.07 _2.157 0.0 80.711 -0.4100 -33.089 Vel = 21.78 19 38 16.80 122.78 2 0.0 9.000 120 53.410 to 0.0 0.0 0.0 20 38 -125.29 2.157 0.0 9.000 -0.1159 -1.043 Vel = 11.00 20 38 16.80 121.57 2 0.0 9.000 120 52.367 to 0.0 0.0 0.0 _21 38 -3.72 2.157 0.0 9.000 -0.0002 -0.002 Vel= 0.33 21 38 16.80 121.57 2 0.0 9.000 120 52.365 to 0.0 0.0 0.0 22 38 117.85 2.157 0.0 9.000 0.1034 0.931 Vel= 10.35 22 38 16.80 122.65 2 X 10.461 82.750 120 53.296 to 0.0 10.461 0.0 23 38 _ 240.5 _2.157 6.0 93:211 Oy3871 36'oS6 vet-`21.1 23 38 0.0 2 T 12.307 2.000 120 89.382 to 0.0 12.307 0.0 24 38 240.5 2.157 0.0 14.307 0.3872 5.539 Vel = 21.12 0.0 24 240.50 94.921 K Factor= 24.69 25 38 34.88 2 T 12.307 2.000 120 93.441 to 0.0 12.307 0.0 26 38 34.88 2.157 0.0 14.307 0.0109 0.156 Vel= 3.06 26 38 0.0 2 2X 20.921 180.000 120 93.597 to 0.0 20.921 0.0 27 38 34.88 2.157 0.0 200.921 _ 0.0109 2.185 Vel = 3.06 27 38 0.0 2 �T 12.307 2.000 120 95.782 to 0.0 12.307 0.0 28 38 34.88 2.157 0.0 14.307 0.0109 0.156 Vel = 3.06 0.0 28 34.88 _ 95.938 K Factor= 3.56 29 38 35.82 2 T 12.307 2.000 120 94.426 to 0.0 12.307 0.0 30 38 35.82 2.157 0.0 14.307 0.0114 0.163 Vel = 3.14 30 38 0.0 2 2X 20.921 180.000 120 94.589 to 0.0 20.921 0.0 31 38 35.82 2.157 0.0 200.921 0.0114 2.296 Vel= 3.14 31 38 0.0 2 T 12.307 2.000 120 96.885 to 0.0 12.307 0.0 32 38 35.82 2.157 - 0.0 _ 14.307 0.0114 0.163 Vel= 3.14 0.0 32 35.82 __ _ 97.048 K Factor= 3.64 33 38 37.93 2 T 12.307 2.000 120 95.257 to 0.0 12.307 0.0 34 38 _ 37.93 2.157 0.0 14.307 0.0127 0.1821Vei_= 3.33 _- 34 38 0.0 2 2X 20.921 180.000 120 95.439 to 0.0 20.921 0.0 35 38 37.93 2.157 0.0 200.921 0.0127 2.552 Vel= 3.33 Computer Programs by Hydratec Inc. Revision: 50.52.1 I Final Calculations - Hazen-Williams S. A. COMUNALE Page 8 SYSTEM 3 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 35 38 0.0 2 T 12.307 2.000 120 97.991 to 0.0 12.307 0.0 36 38 37.93 2.157 0.0 14.307 0.0127 0.182 Vel= 3.33 0.0 36 37.93 98.173 K Factor= 3.83 _ 37 38 41.48 2 T 12.307 2.000 120 96.075 to 0.0 12.307 0.0 38 38 41.48 2.157 0.0 14.307 0.0150 0.214 Vel= 3.64 38 38 0.0 2 2X 20.921 180.000 120 96.289 to 0.0 20.921 0.0 39 38 41.48 2.157 0.0 200.921 0.0150 3.012 Vel= 3.64 39 38 0.0 2 T 12.307 2.000 120 99.301 to 0.0 12.307 0.0 40 38 41.48 2.157 0.0 14.307 0.0150 0.214 Vel= 3.64 0.0 40 41.48 99.515 K Factor= 4.16 41 38 46.13 2 T 12.307 2.000 120 96.796 to 0.0 12.307 0.0 42 38 46.13 2.157 0.0 14.307 0.0182 0.261 Vel= 4.05 42 38 0.0 2 2X 20.921 180.000 120 97.057 to 0.0 20.921 0.0 43 38 46.13 2.157 0.0 200.921 0.0182 3.666 Vel= 4.05 43 38 0.0 2 T 12.307 2.000 120 100.723 to 0.0 12.307 0.0 44 38 46.13 2.157 0.0 14.307 0.0182 0.261 Vel = 4.05 0.0 --v 44 46.13 100.984 K Factor= 4.59 45 38 51.77 2 T 12.307 2.000 120 97.417 to 0.0 12.307 0.0 46 38 51.77 _2.157 0.0 14.307 0.0226 0.323 Vel = 4.55 46 38 0.0 2 2X 20.921 180.000 120 97.740 to 0.0 20.921 0.0 47 38 51.77 2.157 0.0 200.921 0.0226 4._538 Vel= 4.55 _ 47 38 0.0 2 T 12.307 2.000 120 102.278 to 0.0 12.307 0.0 48 38 51.77 2.157 0.0 14.307 0.0226 0.323 Vel = 4.55 0.0 48 _ 51.77 _ 102.601 K Factor= 5.11 49 38 58.29 2 T 12.307 2.000 120 97.933 to 0.0 12.307 0.0 50 38 58.29 2.157 0.0 14.307 0.0282 0.403 Vel= 5.12 50 38 0.0 2 2X 20.921 180.000 120 98.336 to 0.0 20.921 0.0 51 38 58.29 2.15.7 0.0 200.921 _0.0281_ 5.652 Vel= 5_.12_ 51 38 0.0 2 T 12.307 2.000 120 103.988 to 0.0 12.307 0.0 52 38 58.29 2.157 0.0 14.307 0.0281 0.402 Vel= 5.12 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S.A. COMUNALE Page 9 SYSTEM 3 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFacl Pt to or Ftng's Pe *****"' Notes *- `* Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 0.0 52 58.29 104.390 K Factor= 5.71 53 38 65.51 2 T 12.307 2.000 120 98.336 to 0.0 12.307 0.0 54 38 65.51 2.157 0.0 14.307 0.0349 0.499 Vel= 5.75 54 38 0.0 2 2X 20.921 180.000 120 98.835 to 0.0 20.921 0.0 55 38 65.51 2.157 0.0 200.921 0.0349 7.015 Vel= 5.75 55 38 0.0 2 T 12.307 2.000 120 105.850 to 0.0 12.307 0.0 56 65.51 2.157 0.0 14.307 0.0349 0.499 Vel = 5.75 0.0 56 65.51 ____ 106.34_9 K Factor= 6.35 57 38 73.49 2 T 12.307 2.000 120 98.633 to 0.0 58 ..78 73.49 2.157 0.0 14.307 0.0432 0.618 Vel= 6.45 58 36 0.0 2 2X 20.921 180.000 120 99.251 to 0.0 20.921 0.0 59 38 73.49 2.157 0.0 200.921 0.0432 8.678 d = 6.45 59 38 0.0 2 T 12.307 2.000 120 107.9 9 to 0.0 12.307 0.0 60 38 73.49 2.157 0.0 14.307 0.0431 0.617 Vel= 6.45 0.0 60 73.49 108.546 K Factor= 7.05 61 38 82.20 2 T 12.307 2.000 120 98.831 to 0.0 12.307 0.0 62 38 _ 82.2 2.157 0.0 14.307 0.0531 0.760_ Vel= 7.22 _ 62 38 0.0 2 2X 20.921 180.000 120 99.591 to 0.0 20.921 0.0 63 38 _ 82.2 2.157 0.0 200.921 0.0531 10.674 Vel= 7.22 _ 63 38 0.0 2 T 12.307 2.000 120 110.265 to 0.0 12.307 0.0 64 38 82.2 2.157 0.0 14.307 0.0531 0.760 Vel= 7.22 0.0 64 82.20 111.025 K Factor= 7.80 65 38 91.59 2 T 12.307 2.000 120 98.940 to 0.0 12.307 0.0 66 _38 91.59 _2.157_ 0.0 14.307_ 0.0649 0.9_28 Vel= 8.04 66 38 0.0 2 2X 20.921 180.000 120 99.868 to 0.0 20.921 0.0 67 38 91.59 2.157 0.0 200.921 0.0649 13.040 Vel= 8.04 67 38 0.0 2 T 12.307 2.000 120 112.908 to 0.0 12.307 0.0 68 38 91.59 2.157 0.0 14.307 0.0649 0.928 Vel= 8.04 0.0 68 91.59 _ 113.836 _ K Factor=_ 8.58 69 38 123.43 2 T 12.307 2.000 120 98.979 to 0.0 12.307 0.0 70 38 123.43 2.157 0.0 14.307 0.1127 1.612 Vel = 10.84 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 10 SYSTEM 3 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 70i�38 0.0 2 2X 20.921 180.000 120 100.591 to 0.0 20.921 0.0 71 38 123.43 2.157 0.0 200.921 0.1127 22.646 Vel= 10.84 _ 71 ` 38 0.0� 2 T 12.307 2.000 120 123.237 to 0.0 12.307 0.0 72 38 123.43 2.157 0.0 14.307 0.1127 1.613 Vel= 10.84 0.0 72 123.43 124.850 K Factor= 11.05 1 38 247.12 4 0.0 9.500 120 91.717 to 0.0 0.0 0.0 9 38 247.12 4.26 0.0 9.500 0.0147 0.140 Vel= 5.56 9 38 247.33 4 0.0 v9.500 120 91.857 to 0.0 0.0 0.0 17 38 494.45 4.26 0.0 9.500 0.0535 0.508 Vel = 11.13 17 38 248.07 4 0.0 9.500 120 92.365 to 0.0 0.0 0.0 25 38 742.52 4.26 0.0 9.500 0.1133 1.076 Vel= 16.71 25 38 ` -34.88 4 0.0 9.500 120 93.441 to 0.0 0.0 0.0 29 38 707.64 4.26 0.0 9.500 0.1037 0.985 Vel = 15.93 29 38 -35.82 4 0.0 8.833 120 94.426 to 0.0 0.0 0.0 33 38 671.82 4.26 0.0 8.833 0.0941 0.831 Vel = 15.12 33 38 -37.93 4 0.0 9.667 120 95.257 to 0.0 0.0 0.0 37 38 633.89 4.26 0.0 9.667 0.0846 0.818 Vel = 14.27 37 38 -41.47 4 0.0 9.667 120 96.075 to 0.0 0.0 0.0 41 38 592.42 4.26 0.0 9.667 0.0746 0.721 Vel = 13.34 41 _38 -46.14 4 0.0 9.667 120 96.796 to 0.0 0.0 0.0 45 38 546.28 4.26 0.0 9.667_ 0.0642 _0.621 Vel = 12.3_0 45 38 -51.76 4 0.0 9.667 120 97.417 to 0.0 0.0 0.0 49 38 _ 494.52 4.26 0.0 _ 9.667 0.0534 0.516 Vel= 11.13 49 38 -58.29 4 0.0 9.500 120 97.933 to 0.0 0.0 0.0 53 _ 38 436.23 4.26 _ 0.0 9.500 0.0424 0.403 Vel= _9.82 53 38 -65.51 4 0.0 9.500 120 98.336 to 0.0 0.0 0.0 370.72 4.26 0.0 9.500 0.0313 _0.297 Vel= 8.34 57 38 -73.50 4 0.0 9.500 120 `v 98.633 to 0.0 0.0 0.0 61 _ 38 297.22 4.26 0.0 9.500 0.0208 0.198 Vel= 6.69 61 38 -82.20 4 0.0 9.500 --- 120 98.831 _T_-_-- to 0.0 0.0 0.0 65_ _38 _215.02 426 _ 0.0 9.500 0.0115__ 0.109 _Vel = 4.84 65 38 -91.59 4 0.0 9.500 120 98.940 to 0.0 0.0 0.0 69 38 123.43 4.26 0.0 9.500 0.0041 0.039 Val = 2.78 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 11 SYSTEM 3 Date 7.6.18 Node! Elev! K Qa Nom Fitting Pipe CFaci Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 0.0 69 123.43 _ 98.979 K Factor= 12.41 8 38 239.74 4 0.0 9.500 120 94.308 to 0.0 0.0 0.0 16 38 239.74 4.26 0.0 9.500 0.0140 0.133 Vel = 5.40 16 38 239.91 4 0.0 9.500 120 94.441 to 0.0 0.0 0.0 _24 38 479.65 4.26 0.0 9.500 0.0505 0.480 Vel = 10.80 24 38 240.50 4 0.0 9.500 120 94.921 to 0.0 0.0 0.0 28 38 720.15 4.26 0.0 9.500 0.1071 1.017 Vel = 16.21 28 38 34.88 4 0.0 9.500 120 95.938 to 0.0 0.0 0.0 32 38 755.03 4.26 0.0 9.500 0.1168 1.110 Vel= 17.00 32 38 35.82 4 0.0 8.833 120 97.048 to 0.0 0.0 0.0 36 _38 790.85 4.26 0.0 8.833 0.1274 1.125 Vel = 17.80 _ 36 38 37.92 4 0.0 9.667 120 98.173 tG 0.0 0.0 0.0 40 38 828.77 4.26 0.0 9.667 0.1388 1.342 Vel = 18.66 40 38 41.48 4 0.0 9.667 120 99.515 to 0.0 0.0 0.0 44 38_ 870.25 4.26 _ _ 0.0 9.667 0.1520 _ 1.469Vel= 19.59 _ 44 38 46.13 4 0.0 9.667 120 100.984 ` to 0.0 0.0 0.0 48 38 916.38 4.26 0.0 9.667 0.1673 1.617 Vel= 20.63 48 38 51.77 4 0.0 9.667 120 102.601 to 0.0 0.0 0.0 52 38_ _ 968.15 4.26 0.0 9.667 0.1851 1.789 Vel = 21.79 52 `T38 58.29 4 0.0 9.500 120 104.390 to 0.0 0.0 0.0 56 38 _ 1026.44 4.26 _ 0.0 9.500 0.2062 1.959 Vel= 23.10 56 38 65.51 4 - 0.0 9.500 120 106.349 to 0.0 0.0 0.0 60 _ 38 1091.95_ 4.26 _0.0 _ 9.500 0.2313 2.197 Vel = 24.58 60 38 73.49 4 0.0 9.500 120 108.546 to 0.0 0.0 0.0 64 38 1165.44 4.26 0.0 9.500 0.260_9_ 2.479 Vel = 26.23 64 38 82.20 4 - 0.0 9.500 120 111.025 to 0.0 0.0 0.0 _68 38_ 1.247.64 4.26 _ 0.0 9.500_ 0.2959 2.811 Vel =_ 28.08 68 38 91.59 4 T 26.334 6.667 120 113.836 ` to 0.0 26.334 0.0 FMJ 38 1339.234.26_ 0.0_ 33.001 0.3374 _11.134 Vel= 30.15 FMJ 38 -1462.66 4 T 26.334 3.000 120 124.970 to 0.0 26.334 0.0 72 38 -123.43 4.26 0.0 29.334 -0.0041 -0.120 Vel = 2.78 0.0 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams S. A. COMUNALE Page 12 SYSTEM 3 Date 7.6.18 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 72 -123.43 _ 124.850 K Factor= -11.05 _ FMJ 38 1462.67 6 2V 25.147 17.750 120 124.970 to 0.0 25.147 0.0 TR3 38 1462.67 6.357 0.0 42.897 0.0565 2.425 Vel= 14.79 TR3 38 0.0 6 T 37.72 37.000 120 127.395 to 0.0 37.720 16.592 * Fixed Loss= 1 BR3 2 1462.67 6.357 0.0 74.720 0.0565 4.224 Vel = 14.79 _ BR3 2 H100 100.00 8 T 41.108 2.000 120 148.211 to 0.0 41.108 0.0 LI 2 1562.67 8.249, 0.0 43.108_ 0.0180 0.775 Vel= 9.38 LI 2 0.0 12 5L 99.669 830.000 150 148.986 to F 14.397 120.710 0.0 U_G 2 1562.67 11.2 G 6.645 950.710 0.0027 2.549 Vel = 5.09 UG 2 H150 150.00 10 S 61.525 15.000 150 151.535 to B 21.254 100.677 0.0 PO 2 1712.67 9.42 L 17.898 115.677 0.0074 0.853 Vel = 7.88 0.0 J --- PO 1712.67 152.388 K Factor= 138.74 Computer Programs by Hydratec Inc. Revision: 50.52.1 AutoPeaking Summary S. A. COMUNALE Page 13 SYSTEM 3 Date 7.6.18 Auto Peaking Summary- List or Pipes for Area Calculated Left Right Side Side From To Length From To Length 2 3 70.250 6 7 82.750 10 11 70.250 14 15 82.750 18 19 70.250 22 23 82.750 Flow Safety Pressure Required Margin Differential Left 9.000 1 1712.857 12.768 -0.323 Area Calculated 1712.666 12.444 0.000 Right 9.000 1712.684 12.487 -0.043 Typical Distance Between Heads = 9.000 Split Point Used in Worst Area Peaked = 5 i Computer Programs by Hydratec Inc. Revision: 50.52.1 SA Comunale Page 1 Quell System 1 Date 3.1.18 Hydraulic Design Information Sheet Name - Aldi South Windsor Date - 3 .1.18 Location - 295 Rye Street, South Windsor, CT Building - System No. - 1 Contractor - SA Comunale Contract No. - 57748-018 Calculated By - Brian Maciejewski Drawing No. - 2 Construction: ( ) Combustible x Non-Combustible _( ) ust ble Ceiling Height 38.5 Occupancy - High Piled Storage S (x) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( } 3 ( ) Ex.Haz. Y ( ) Figure Curve S Other T Specific Ruling Tyco Quell data, dwg l Made By Date E M No. of Ultra K17 Sprinklers - 25 System Type Sprinkler/Nozzle End Head Pressure (PSI) - ( ) Wet Make Tyco D Sprinkler K-Factor - 16.8 ( ) Dry Model Ultra K17 E Elevation at Highest Outlet - 39 ( ) Deluge Size 3/4 S Hose Allowance - Inside - (x) Preaction K-Factor 16.8 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.286 G Hose Allowance - Outside - 500 N Note Calculation Flow Required - 2879.19 Press Required - 135.56 PO Summary C-Factor Used: 100 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - Cap. - T Time of Test - Rated Cap. - 2500 Elev.- E Static Press - @ Press - 150 R Residual Press - Elev. - 0 Well Flow - Proof Flow S Elevation - 2 U P Location - Fire Pump House (see dwg 5) P L Source of Information - Y C Commodity Class Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled o Palletized % Rack M ( ) Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Encap. S R ( ) Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( ) Mult. Row ( ) Open Shelf O C i��rs�a�e.rctff►f�rtr. R K Flue Spacing Clearance:Storage to Ceiling ,' A Longitudinal Transverse �`'��'.; y�► ,�` �� E Horizontal Barriers Provided: .ifs r;ii:itje Water Supply Curve C SA Comunale Page 2 Date 3.1.18 Quell System 1 Pump Data: Demand: P1 -Pump Churn Pressure 177 D1 - Elevation 16.025 P2- Pump Rated Pressure 160 D2-System Flow :2379.19 P2 - Pump Rated Flow 2000 D2 - System Pressure : 135.559 P3- Pump Pressure @ Max Flow 120 Hose ( Demand ) : 500 P3- Pump Max Flow 3750 D3- System Demand :2879.19 Safety Margin 6.999 180 Pi 168 P2 156 P 144 D2 R 132 pg D3 E 120 S 108 S 96 U 84 R 72 E 60 48 36 24 12 400 800 1200 1600 2000 2400 2800 3200 3600 FLOW ( NA1.85 ) r r7,nmr1der Programs by Hvdratec Inc, Revision:' 50 F? 1 Fittings Used Summary SA Comunale Quell System 1 Page 3 Date 3.1.18 Fitting Legend Abbrev. Name �/2 3/4 1 1�/ 11/2 2 2�/2 3 3�/2 4 5 6 8 10 12 14 16 18 20 24 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 F NFPA 13 45'Elbow 1 1 1 1 2 2 3 3 3 4 5 7 9 11 13 17 19 21 24 28 G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 L NFPA 13 Long Turn Elbow 0.5 1 2 2 2 3 4 5 5 6 8 9 13 16 18 24 27 30 34 40 S NFPA 13 Swing Check 0 0 5 7 9 11 14 16 19 22 27 32 45 55 65 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 V 90'Ell Firelock#001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 4.5 5.1 0 0 0 0 0 Unit Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *. The fittings marked with a *show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a *will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Revision: 50.52.1 Pressure/ Flow Summary - STANDARD SA Comunale Page 4 Quell System 1 Date 3.1.18 Node Elevation. K-Fact Pt Pn Flow Density Area Press No Actual Actual Reg. 1 39.0 16.8 30.0 na 92.02 0.1 100 30.0 2 39.0 16.8 30.33 na 92:52 0.1 100 30.0 3 39.0 16.8 31.39 na 94.13 0.1 100 30.0 4 39.0 16.8 32.65 na 96.0 0.1 100 30.0 5 39.0 16.8 32.99 na 96.49 0.1 100 30.0 6 39.0 16.8 30.07 na 92.13 0.1 100 30.0 7 39.0 16.8 30.4 na 92.63 0.1 100 30.0 8 39.0 16.8 31.47 na 94.24 0.1 100 30.0 9 39.0 16.8 32.73 na 96.11 0.1 100 30.0 10 39.0 16.8 33.06 na 96.6 0.1 100 30.0 11 39.0 16.8 30.32 na 92.5 0.1 100 30.0 12 39.0 16.8 30.65 na 93.01 0.1 100 30.0 13 39.0 16.8 31.73 na 94.63 0.1 100 30.0 14 39.0 16.8 32.99 na 96.5 0.1 100 30.0 15 39.0 16.8 33.33 na 97.0 0.1 100 30.0 16 39.0 16.8 30.86 na 93.32 0.1 100 30.0 17 39.0 16.8 31.19 na 93.83 0.1 100 30.0 18 39.0 16.8 32.29 na 95.46 0.1 100 30.0 19 39.0 16.8 33.58 na 97.35 0.1 100 30.0 20 39.0 16.8 33.92 na 97.85 0.1 100 30.0 21 39.0 16.8 31.78 na 94.71 0.1 100 30.0 22 39.0 16.8 32.13 na 95.22 0.1 100 30.0 23 39.0 16.8_ 33.25 na 96.87_ _ 0.1 100 __ 30.0_ 24 39.0 16.8 34.58 na 98.79 0.1 100 30.0 25 39.0 16.8 34.93 na 99.29 0.1 100 30.0 100 0.0 52.27 na 101 0.0 52.36 na 102 0.0 52.64 na 103 0.0 53.27 na 104 0.0 54.35 na 200 0.0 56.4 na 201 0.0 56.49 na 202 0.0 56.81 na 203 0.0 57.51 na 204 0.0 58.7 na RDCR 0.0 100.66 na 300 0.0 102.9 na 301 0.0 105.32 na 302 0.0 107.21 na TOR 35.0 97.55 na BOR 2.0 122.38 na UG3 -5.0 127.17 na 500.0 UG4 -5.0 128.88 na UG5 2.0 133.33 na PO 2.0 135.56 na The maximum velocity is 24.05 and it occurs in the pipe between nodes 204 and RDCR Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line SA Comunale Quell System 1 Page 5 Date 3.1.18 Ref Press K Flow Flow Pipe Pipe Fit Fit Tot C Pf Tot Elev Fixed Next Next Pt. Total Fact. Added Total Vel Diam. Length Sum. Length Len Fac perUL Pf Press Loss Press Ref 1 30.000 16.80 92.02 92.02 5.41 2.635 9.500 2 30.329 16.80 92.52 184.54 10.86 2.635 8.500 0.0 9.500 100 0.0346 0.329 0.0 0.0 30.329 2 3 31.394 16.80 94.13 278.67 16.40 2.635 3.083 1 T 111.757 14.840 100 0.2688 3.98916.891 0.0 100 52.274 38.54 0.0 278.67 52.274 100 4 32.650 16.80 96.00 96.0 5.65 2.635 9.000 5 32.987 16.80 96.49 192.49 11.32 2.635 5.917 1 T 111.757 17.674 100 0.11356 2.39616.891 0.0 7 100 52.274 26.62 0.0 192.49 52.24 100 6 30.070 16.80 92.13 92.13 5.42 2.635 9.500 7 30.400 16.80 92.62 184.75 10.87 2.635 8.500 0.0 9.500 100 0.0347 0.330 0.0 0.0 30.400 7 8 31.468 16.80 94.25 279.0 16.41 2.635 3.083 1 T 111.7757 14.840 100 0.2693 3.99716.891 0.0 8 101 52.356 38.56 0.0 279.00 52.35601 9 32.726 16.80 96.11 96.11 5.65 2.635 9.000 0.0 9.000 100 0.0376 0.338 0.0 0.0 33.064 10 10 33.064 16.80 96.60 192.71 11.34 2.635 5.917 1 T 11.757 17.674 100 0.1358 2.40116.891 0.0 101 52.356 26.63 0.0 192.71 52.356 101 11 30.317 16.80 92.50 92.5 5.44 2.635 9.500 0.0 9.500 100 0.0349 0.332 0.0 0.0 30.649 12 12 30.649 16.80 93.01 185.51 10.91 2.635 8.500 0.0 8.500 100 0.1266 1.076 0.0 0.0 31.725 13 13 31.725 16.80 94.63 280.14 16.48 2.635 3.083 1 T 11.757 14.840 100 0.2714 4.02816.891 0.0 102 52.644 38.61 0.0 280.14 52.644 102 14 32.994 16.80 96.50 96.5 5.68 2.635 9.000 0.0 9.000 100 0.0378 0.340 0.0 0.0 33.334 15 15 33.334 16.80 97.00 193.5 11.38 2.635 5.917 1 T 102 52.644 26.67 0.0 193.50 11.757 17.674 100 0.1369 2.41916.891 0.0 52.644 102 16 30.857 16.80 93.32 93.32 5.49 2.635 9.500 0.0 9.500 100 0.0355 0.337 0.0 0.0 31.194 17 17 31.194 16.80 93.83 187.15 11.01 2.635 8.500 0.0 8.500 100 0.1287 1.094 0.0 0.0 32.288 18 18 32.288 16.80 95.46 282.61 16.63 2.635 3.083 1 T 11.757 14.840 100 0.2758 4.09316.891 0.0 53.272 103 103 53.272 38.72 0.0 282.61 19 33.577 16.80 97.35 97.35 5.73 2.635 9.000 0.0 9.000 100 0.0384 0.346 0.0 0.0 33.923 20 20 33.923 16.80 97.85 195.2 11.48 2.635 5.917 1 T 11.757 17.674 100 0.1391 2.45816.891 0.0 53.272 103 103 53.272 26.74 0.0 195.20 21 31.780 16.80 94.71 94.71 5.57 2.635 9.500 0.0 9.500 100 0.0365 0.347 0.0 0.0 32.127 22 22 32.127 16.80 95.22 189.93 11.17 2.635 8.500 0.0 8.500 100 0.1322 1.124 0.0 0.0 33.251 23 23 33.251 16.80 96.88 286.81 16.87 2.635 3.083 1 T 104 54.348 38.90 0.0 286.81 11.757 14.840 100 0.2834 4.20616.891 0.0 54.348 104 24 34.576 16.80 98.79 98.79 5.81 2.635 9.000 0.0 9.000 100 0.0394 0.355 0.0 0.0 34.931 25 25 34.931 16.80 99.29 198.08 11.65 2.635 5.917 1 T 11.757 17.674 100 0.1429 2.52616.891 0.0 54.348 104 104 54.348 26.87 0.0 198.08 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line Page 6 SA Comunale Date 3.1.18 Quell System 1 Ref Press K Flow Flow Pipe Pipe Fit Fit Tot C Pf Length Len Fac perUL Tot Elev Pf Press Fixed Lo s Press Ref Next Pt. Total Fact. Added Total Vel Diam. Length Sum g 100 52.274 471.16 471.16 18.11 3.26 2.000 1 T 14.387 16.387 100 0.2518 4.126 0.0 0.0 56.400 200 200 56.400 62.74 0.0 471.16 101 52.356 471.70 471.7 18.13 3.26 2.000 1 T 14.387 16.387 100 0.2523 4.135 0.0 0.0 56.491 201 201 56.491 62.76 0.0 471.70 102 52.644 473.63 473.63 18.21 3.26 2.000 1 T 14.387 16.387 100 0.2543 4.167 0.0 0.0 56.81'1 202 202 56.811 62.84 0.0 473.63 103 53.272 477.81 477.81 18.37 3.26 2.000 1 T 14.387 16.387 100 0.2584 4.235 0.0 0.0 57.507 203 203 57.507 63.01 0.0 477.81 104 54.348 484.89 484.89 18.64 3.26 2.000 1 T 14.387 16.387 100 0.2656 4.352 0.0 0.0 58.700 204 204 58.700 63.29 0.0 484.89 200 56.400 471.16 471.16 4.76 6.357 9.333 0.0 9.333 100 0.0098 0.091 0.0 0.0 56.49*1 201 201 56.491 471.70 942.86 9.53 6.357 9.083 0.0 9.083 100 0.0352 0.320 0.0 0.0 56.811 202 202 56.811 473.63 1416.49 14.32 6.357 9.333 0.0 9.333 100 0.0746 0.696 0.0 0.0 57.507 203 203 57.507 477.81 1894.3 19.15 6.357 9.333 0.0 9.333 100 0.1278 1.193 0.0 0.0 58.700 204 204 58.700 484.89 2379.19 24.05 6.357 215.330 0.0 215.330 100 0.1948 41.957 0.0 0.0 100.657 RDCR RDCR 00.657 0.0 2379.19 14.28 8.249 30.000 1 V 10.897 40.897 100 0.0548 2.240 0.0 0.0 102.897 300 300 102.897 234.55 0.0 2379.19 300 102.897 2379.19 2379.19 14.28 8.249 44.167 0.0 44.167 100 0.0548 2.420 0.0 0.0 107. 301 301 105.317 0.0 2379.19 14.28 8.249 23.667 1 V 10.897 344.564 100 0.0548 1.893 0.0 0.0 10 .2110 302 302 107.210 0.0 2379.19 14.28 8.249 67.750 3V 32.691 100.441 100 0.0548 5.50315.158 0.0 97.555 TOR TOR 97.555 240.88 0.0 2379.19 TOR 97.555 2379.19 2379.19 14.28 8.249 32.000 1S2B1T4# 87.176 119.176 100 0.0548 6.52914.292 4.000 122.376 BOR BOR 122.376 0.0 2379.19 14.28 8.249 4.000 1 T 41.108 45.108 120 0.0391 1.763 3.032 0.0 127.171 UG3 UG3 127.171 H500 500.00 2879.19 13.25 9.42 15.000 1 L1 T 73.829 88.829 150 0.0193 1.714 0.0 0.0 128.885 UG4 UG4 128.885 0.0 2879.19 13.25 9.42 280.000 51-1 F1 G 107.388 387.388 150 0.0193 7.474-3.032 0.0 133.327 UG5 UG5 133.327 0.0 2879.19 13.25 9.42 15.000 1 S1 B1 L 100.677 115.677 150 0.0193 2.232 0.0 0.0 135.559 PO PO 135.559 247.29 0.0 2879.19 Cc)mpctt,,r rrr-qr^ms hNt Hvdratec Inn SA Comunale Page 1 Quell System 2 Date 3.1.18 Hydraulic Design Information Sheet Name - Aldi South Windsor Date - 3 .1.18 Location - 295 Rye Street, South Windsor, CT Building - System No. - 2 Contractor - SA Comunale Contract No. - 57748-018 Calculated By - Brian Maciejewski Drawing No. - 3 Construction: ( ) Combustible (x) Non-Combustible Ceiling Height - 38.5 Occupancy - High Piled Storage S (x) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y ( ) Figure Curve S Other T Specific Ruling Tyco Quell data, dwg 1 Made By Date E M No. of Ultra K17 Sprinklers - 25 System Type Sprinkler/Nozzle End Head Pressure (PSI) - ( ) Wet Make Tyco D Sprinkler K-Factor - 16.8 ( ) Dry Model Ultra K17 E Elevation at Highest Outlet - 38.5 ( ) Deluge Size 3/4 S Hose Allowance - Inside - (x) Preaction K-Factor 16.8 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.286 G Hose Allowance - Outside - 500 N Note Calculation Flow Required - 2893.17 Press Required - 136.54 PO Summary C-Factor Used: 100 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - Cap. - T Time of Test - Rated Cap. - 2500 Elev. - E Static Press - @ Press - 150 R Residual Press - Elev. - 0 Well Flow - Proof Flow S Elevation - 2 U P Location - Fire Pump House (see dwg 5) P L Source of Information - Y C Commodity Class Location O Storage Ht. Area Aisle W. M Storage Method: Solid Piled a Palletized o Rack M ( ) Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Encap. - S R ( ) Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( ) Mult. Row ( ) Open Shelf R K Flue Spacing Clearance:Stora e to Cei1in A Longitudinal Transverse g g ��.'��� «' :h>�`s''`•` E Horizontal Barriers Provided: } 00. 27t4 + ,;s Water Supply Curve C SA Comunale Page 2. Quell System 2 Date 3.1.18 Pumpp Data: Demand: P1 - Pump Churn Pressure 177 D1 - Elevation 15.808 P2- Pump Rated Pressure 160 D2- System Flow : 2393.7 P2 - Pump Rated Flow 2000 D2-System Pressure : 136.539 P3- Pump Pressure @ Max Flow 120 Hose ( Demand ) : 500 P3- Pump Max Flow 3750 D3-System Demand :2893.7 Safety Margin 5.717 180 168 156 P 144 R 132 P3 D3 E 120 S 108 S 96 U 84 R 72 E 60 48 36 24 12 400 800 1200 1600 2000 2400 2800 ! 3200 3600 FLOW ( NA1.85 ) ('nmputnr n>>Hvdratec Inc. Pay 1^inn• r2 1 Fittings Used Summary SA Comunale Quell System 2 Page 3 Fitting Legend Date 3.1.18 Abbrey._ Name '/2 3/4 1 1'/4 1'/2 2 2'/2 3 3'/2 4 5 6 8 10 12 14 16 18 20 24 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 F NFPA 13 45'Elbow 1 1 1 1 2 2 3 G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 3 3 4 5 7 4 5 6 7 13 7 19 21 24 28 L NFPA 13 Long Turn Elbow 0.5 1 2 2 8 10 11 13 S NFPA 13 Swing Check 0 0 5 7 9 11 14 16 19 22 27 32 45 55 65 24 27 30 34 40 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 u 45'Ell Firelock#003 0 0 0 0 0 1.8 2.2 2.6 0 3.4 4.2 5 5 2.8 3.2 0 0 0 0 0 V 90'Ell Firelock#001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 4.5 5.1 0 0 0 0 0 x 90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 21 25 33 9.3 11 0 0 0 0 0 Unit Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *. The fittings marked with a*show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a*will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Revision: 50.52.1 Pressure/ Flow Summary - STANDARD SA Comunale Page 4 Quell System 2 Date 3.1.18 Node Elevation K-Fact Pt Pn Flow Density Area Press No Actual Actual Reg. 1 38.5 16.8 30.0 na 92.02 0.1 100 30.0 2 38.5 16.8 30.31 na 92.49 0.1 100 30.0 3 38.5 16.8 31.5 na 94.29 0.1 100 30.0 4 38.5 16.8 33.59 na 97.37 0.1 100 30.0 5 38.5 16.8 33.92 na 97.85 0.1 100 30.0 g 38.5 16.8 30.07 na 92.12 0.1 100 30.0 7 38.5 16.8 30.38 na 92.6 0.1 100 30.0 8 38.5 16.B 31.58 na 94.4 0.1 100 30.0 38.5 16.8 33.67 na 97.49 0.1 100 30.0 g 9 38 5 16.8 34.0 na 97.96 0.1 100 30.0 10 11 38.5 16.8 30.32 na 92.51 0.1 100 30.0 12 38.5 16.8 30.64 na 92.99 0.1 100 30.0 13 38.5 16.8 31.84 na 94.8 0.1 100 30.0 14 38.5 16.8 33.95 na 97.89 0.1 100 30.0 5 38.5 16.8 34.28 na 98.37 0.1 100 30.0 1 1 38.5 16.8 30.86 na 93.33 0.1 100 30.0 31.18 na 93.81 0.1 100 30.0 17 38.5 16.8 32.4 na 95.63 0.1 100 30.0 18 38.5 16.8 1 g 38 5 16.8 34.55 na 9B.75 0.1 100 30.0 20 38.5 16.8 34.88 na 99.23 0.1 100 30.0 21 38.5 16.8 31.78 na 94.7 0.1 100 30.0 22 38.5 16.8 32.11 na 95.19 0.1 100 30.0 23 38.5 16.8_ . 33.36 __ na 97.04 0.1 100 30.0 24 38.5 16.B _ 35.57 na 100.2 0.1 _100 - . _ . 30.0. 25 38.5 16.8 35.91 na 100.68 0.1 100 30.0 100 38.5 36.03 na 101 38.5 36.11 na 102 38.5 36.41 na 103 38.5 37.05 na 104 38.5 38.14 na 200 38.5 40.21 na 201 38.5 40.3 na 202 38.5 40.63 na 203 38.5 41.33 na I 204 38.5 42.54 na j RDCR 38.5 75.12 na 300 38.5 80.57 na TOR 30.0 90.22 na ] BOR 2.0 112.56 na RM2 2.0 113.32 na RM1 2.0 128.98 na UG 2.0 134.29 na 500.0 PO 2.0 136.54 na The maximum velocity is 24.2 and it occurs in the pipe between nodes 204 and RDCR Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line SA Comunale Quell System 2 Page 5 Date 3.1.18 Ref Press K Flow Flow Pipe Pipe Fit Fit Tot C Pf Tot Elev Fixed Next Next Pt. Total Fact. Added Total Vel Diam. Length Sum. Length Len Fac perUL Pf Press Loss Press Ref 1 30.000 16.80 92.02 92.02 5.41 2.635 9.000 0.0 9.000 100 0.0346 0.311 0.0 0.0 30.311 2 2 30.311 16.80 92.49 184.51 10.86 2.635 9.500 0.0 9.500 100 0.1254 1.191 0.0 0.0 31.502 3 3 31.502 16.80 94.29 278.8 16.40 2.635 5.083 1 T 11.757 16.840 100 0.2690 4.530 0.0 0.0 36.032 100 100 36.032 46.45 0.0 278.80 4 33.594 16.80 97.37 97.37 5.73 2.635 8.500 0.0 8.500 100 0.0385 0.327 0.0 0.0 33.921 5 5 33.921 16.80 97.85 195.22 11.49 2.635 3.417 1 T 11.757 15.174 100 0.1391 2.111 0.0 0.0 36.032 100 100 36.032 32.52 0.0 195.22 6 30.070 16.80 92.12 92.12 5.42 2.635 9.000 0.0 9.000 100 0.0347 0.312 0.0 0.0 30.382 7 7 30.382 16.80 92.61 184.73 10.87 2.635 9.500 0.0 9.500 100 0.1256 1.193 0.0 0.0 31.575 8 8 31.575 16.80 94.40 279.13 16.42 2.635 5.083 1 T 11.757 16.840 100 0.2696 4.540 0.0 0.0 36.115 101 101 36.115 46.45 0.0 279.13 9 33.672 16.80 97.49 97.49 5.74 2.635 8.500 0.0 8.500 100 0.0385 0.327 0.0 0.0 33.999 10 10 33.999 16.80 97.95 195.44 11.50 2.635 3.417 1 T 11.757 15.174 100 0.1394 2.116 0.0 0.0 36.115 101 101 36.115 32.52 0.0 195.44 11 30.323 16.80 92.51 92.51 5.44 2.635 9.000 0.0 9.000 100 0.0349 0.314 0.0 0.0 30.637 12 12 30.637 16.80 92.99 185.5 10.91 2.635 9.500 0.0 9.500 100 0.1266 1.203 0.0 0.0 31.840 13 13 31.840 16.80 94.80 280.3 16.49 2.635 5.083 1 T 11.757 16.840 100 0.2716 4.574 0.0 0.0 36.414 102 102 36.414 46.45 0.0 280.30 14 33.953 16.80 97.89 97.89 5.76 2.635 8.500 0.0 8.500 100 0.0387 0.329 0.0 0.0 34.282 15 15 34.282 16.80 98.37 196.26 11.55 2.635 3.417 1 T 11.757 15.174 100 0.1405 2.132 0.0 0.0 36.414 102 102 36.414 32.52 0.0 196.26 16 30.859 16.80 93.33 93.33 5.49 2.635 9.000 0.0 9.000 100 0.0356 0.320 0.0 0.0 31.179 17 17 31.179 16.80 93.80 187.13 11.01 2.635 9.500 0.0 9.500 100 0.1286 1.222 0.0 0.0 32.401 18 18 32.401 16.80 95.63 282.76 16.64 2.635 5.083 1 T 11.757 16.840 100 0.2761 4.649 0.0 0.0 37.050 103 103 37.050 46.45 0.0 282.76 19 34.549 16.80 98.75 98.75 5.81 2.635 8.500 0.0 8.500 100 0.0394 0.335 0.0 0.0 34.884 20 20 34.884 16.80 99.22 197.97 11.65 2.635 3.417 1 T 11.757 15.174 100 0.1427 2.166 0.0 0.0 37.050 103 103 37.050 32.52 0.0 197.97 21 31.778 16.80 94.70 94.7 5.57 2.635 9.000 0.0 9.000 100 0.0364 0.328 0.0 0.0 32.106 22 22 32.106 16.80 95.20 189.9 11.17 2.635 9.500 0.0 9.500 100 0.1322 1.256 0.0 0.0 33.362 23 23 33.362 16.80 97.04 286.94 16.88 2.635 5.083 1 T 11.757 16.840 100 0.2837 4.778 0.0 0.0 38.140 104 104 38.140 46.46 0.0 286.94 24 35.570 16.80 100.20 100.2 5.90 2.635 8.500 0.0 8.500 100 0.0405 0.344 0.0 0.0 35.914 25 25 35.914 16.80 100.68 200.88 11.82 2.635 3.417 1 T 11.757 15.174 100 0.1467 2.226 0.0 0.0 38.140 104 104 38.140 32.53 0.0 200.88 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line SA Comunale Page 6 Quell System 2 Date 3.1.18 Ref Press K Flow Flow Pipe Pipe Fit Fit Tot C Pf Tot Elev Fixed Next Next Pt. Total Fact. Added Total Vel Diam. Length Sum. Length Len Fac perUL Pf Press Loss Press Ref 100 36.032 474.02 474.02 18.22 3.26 2.000 1 T 14.387 16.387 100 0.2547 4.173 0.0 0.0 40.205 200 200 40.205 74.76 0.0 474.02 101 36.115 474.57' 474.57 18.24 3.26 2.000 1 T 14.387 16.387 100 0.2552 4.182 0.0 0.0 40.297 201 201 40.297 74.76 0.0 474.57 102 36.414 476.56 476.56 18.32 3.26 2.000 1 T 14.387 16.387 100 0.2572 4.215 0.0 0.0 40.629 202 202 40.629 74.77 0.0 476.56 103 37.050 480.73 480.73 18.48 3.26 2.000 1 T 14.387 16.387 100 0.2614 4.284 0.0 0.0 41.334 203 203 41.334 74.77 0.0 480.73 104 38.140 487.81 487.81 18.75 3.26 2.000 1 T 14.387 16.387 100 0.2685 4.400 0.0 0.0 42.540 204 204 42.540 74.79 0.0 487.81 200 40.205 474.02 474.02 4.79 6.357 9.333 0.0 9.333 100 0.0099 0.092 0.0 0.0 40.297 201 201 40.297 474.58 948.6 9.59 6.357 9.333 0.0 9.333 100 0.0356 0.332 0.0 0.0 40.629 202 202 40.629 476.55 1425.15 14.41 6.357 9.333 0.0 9.333 100 0.0755 0.705 0.0 0.0 411.334 203 203 41.334 480.74 1905.89 19.27 6.357 9.333 0.0 9.333 100 0.1292 1.206 0.0 0.0 42.540 204 204 42.540 487.81 2393.7 24.20 6.357 165.333 0.0 165.333 100 0.1971 32.579 0.0 0.0 75.119 RDCR RDCR 75.119 0.0 2393.7 14.37 8.249 70.667 1 X 27.662 98.329 100 0.0554 5.448 0.0 0.0 80.567 300 300 80.567 266.68 0.0 2393.70 300 80.567 2393.70 2393.7 14.37 8.249 75.000 3V 32.691 107.691 100 0.0554 5.967 3.681 0.0 90.215 TOR TOR 90.215 252.02 0.0 2393.70 TOR 90.215 2393.70 2393.7 14.37 8.249 25.000 1S2B1T4# 87.176 112.176 100 0.0554 6.21512.127 4.000 112.557 BOR BOR 112.557 0.0 2393.7 14.37 8.249 4.000 1 V 15.269 19.269 120 0.0395 0.762 0.0 0.0 113.319 RM2 RM2 113.319 0.0 2393.7 14.37 8.249 329.000 4V1 U 66.947 395.947 120 0.0395 15.656 0.0 0.0 128.975 RM1 RM1 128.975 0.0 2393.7 11.02 9.42 280.000 51-1 F1 G 107.388 387.388 150 0.0137 5.311 0.0 0.0 134.2813 UG UG 134.286 H500 500.00 2893.7 13.32 9.42 15.000 1 S1 B1 L 100.677 115.677 150 0.0195 2.253 0.0 0.0 136.539 PO PO 136.539 247.64 0.0 2893.70 f'nrni-Mer Prnnrams by Hvdratec Inc. Rpvisinn` 50 52..1 ,.t SA Comunale Page 1 Quell System 3 Date 3.1.18 Hydraulic Desiqn Information Sheet Name - Aldi South Windsor Date - 3.1.18 Location - 295 Rye Street, South Windsor, CT Building - System No. - 3 Contractor - SA Comunale Contract No. - 57748-018 Calculated By - Brian Maciejewski Drawing No. - 3 Construction: ( ) Combustible (x) Non-Combustible Ceiling Height - 38.5 Occupancy - High Piled Storage S (x) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y ( ) Figure Curve S Other T Specific Ruling Tyco Quell data, dwg 1 Made By Date E M No. of Ultra K17 Sprinklers - 25 System Type Sprinkler/Nozzle End Head Pressure (PSI) - ( ) Wet Make Tyco D Sprinkler K-Factor - 16.8 ( ) Dry Model Ultra K17 E Elevation at Highest Outlet - 38.5 ( ) Deluge Size 3/4 S Hose Allowance - Inside - (x) Preaction K-Factor 16.8 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.286 G Hose Allowance - Outside - 500 N Note Calculation Flow Required - 2909.47 Press Required - 126.85 PO Summary C-Factor Used: 100 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - Cap. - T Time of Test - Rated Cap. - 2500 Elev.- E Static Press - @ Press - 150 R Residual Press - Elev. - 0 Well Flow Proof Flow S Elevation - 2 U P Location - Fire Pump House (see dwg 5) P L Source of Information - Y C Commodity Class Location O Storage Ht. Area Aisle W. M Storage Method: Solid Piled o Palletized % Rack M ( ) Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Encap. S R ( ) Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( ) Mult. Row ( ) Open Shelf R K Flue Spacing Clearance:Storage to Ceiling,'.',,.-.-"' A Longitudinal Transverse y� •'°P 7 y E Horizontal Barriers Provided: ' Af0. 7 rm 341 Water Supply Curve C SA Comunale Page 2. Quell System 3 Date 3.1.18 Pump Data: Demand: P1 - Pump Churn Pressure 177 D1 - Elevation 15.808 P2 - Pump Rated Pressure 160 D2- System Flow :2409.47 P2-Pump Rated Flow 2000 D2 -System Pressure : 126.853 P3 - Pump Pressure @ Max Flow 120 Hose ( Demand ) : 500 P3- Pump Max Flow 3750 D3- System Demand :2909.47 Safety Margin 15.072 180 168 156 p 144 R 132 B2 P3 E 120 D3 S 108 S 96 U 84 R 72 E 60 48 36 24 12 400 800 1200 1600 2000 2400 2800 3200 3600 FLOW ( NA1.85 ) CornputPr Prnrtrams hy Hvrlrater. Inc Revision: 50 59 1 Fittings Used Summary SA Comunale Quell System 3 Page 3 Fitting Legend Date 3.1.18 Abbrev._ Name �/2 3/4 1 1�� 1�/2 2 � 2/x 3 3�/z 4 5 6 8 10 12 14 16 18 20 24 _ B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 F NFPA 13 45'Elbow 1 1 1 1 2 2 3 30 3 42 5 70 12 19 21 0 0 0 0 0 9 11 13 17 19 G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 21 24 28 L NFPA 13 Long Turn Elbow 0.5 1 2 2 2 2 3 4 5 6 7 8 10 11 13 S NFPA 13 Swing Check 0 0 3 4 5 5 6 8 9 13 16 5 7 9 11 14 18 24 27 30 34 40 T NFPA 13 90'Flow thru Tee g 4 16 19 22 27 32 45 55 65 45'Ell Firelock#003 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Ll V 45'Ell Firelock#001 0 0 0 0 0 1.8 2.2 2.6 0 3.4 4.2 5 5 2.8 3.2 0 0 0 0 0 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 4.5 5.1 0 0 0 0 0 Unit Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *. The fittings marked with a*show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a*will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Revision: 50.52.1 Pressure / Flow Summary - STANDARD Page 4 SA Comunale Date 3.1.13 Quell System 3 Pt Pn Flow Density Area Press Node Elevation K Fact Actual Actual Re . 30.0 na 92.02 0.1 100 30.0 1 38.5 16.8 100 30.0 2 38.5 16.8 30.35 na 94.25 0.1 3 38.5 16.8 31.47 na 94.25 0.1 100 30.0 4 38.5 16.8 34.66 na 98.91 0.1 100 30.0 35.06 na 99.47 0.1 100 30.0 5 38.5 16.8 30.07 na 92.12 0.1 100 30. g 38.5 16.8 30.42 na 92.65 0.1 100 30.0 7 38.5 16.8 100 30.0 8 38.5 16.8 31.55 na 94.36 0.1 g 38.5 16.8 34.74 na 99.02 0.1 100 30.0 10 38.5 16.8 35.14 na 99.59 0.1 100 30.0 11 38.5 16.8 30.32 na 92.51 0.1 100 30.0 12 38.5 16.8 30.67 na 93.04 0.1 100 30.0 13 38.5 16.8 31.81 na 94.75 0.1 100 30.0 35.03 na 99.43 0.1 100 30.0 14 38.5 16.8 35.43 na 100.0 0.1 100 30.0 15 38.5 16.8 30.85 na 93.31 0.1 100 30.0 16 38.5 16.8 17 38.5 16.8 31.21 na 93.85 0.1 100 30.0 18 38.5 16.8 32.36 na 95.57 0.1 100 30.0 1 g 38.5 16.8 35.64 na 100.29 0.1 100 30.0 i na 100.86 0.1 100 30.0 20 38.5 16.8 36.04 21 38.5 16.8 31.76 na 94.68 0.1 100 30.0 32.13 na 95.22 0.1 100 30.0 22 38.5 16.8 23 38.5 16.8 33.31 na 96.97 0.1 100 30.0 24 38.5 16.8 36.68 na 101.74 0.1 100_ 30.0 25 38.5 16.8 37.09 na 102.32 0.1 100 30.0 100 38.5 36.95 na 101 38.5 37.03 na 102 38.5 37.33 na 103 38.5 37.98 na 104 38.5 39.08 na 200 38.5 41.17 na 201 38.5 41.26 na 202 38.5 41.6 na a 203 38.5 42.31 na 204 38.5 43.54 na RDCR 38.5 64.01 na 300 38.5 74.3 na TOR 35.0 78.0 na BOR 2.0 102.58 na RM2 2.0 103.35 na RM1 2.0 119.2 na UG 2.0 124.58 na 500.0 PO 2.0 126.85 na l The maximum velocity is 24.36 and it occurs in the pipe between nodes 204 and RDCR Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line SA Comunale Quell System 3 Page 5 Date 3.1.18 Ref Press K Flow Flow Pipe Pipe Fit Pt. Total Fact. Added Total Vel Diam. Length Sumixed . Length Len F c perUL Tot Pf Press Next Press Ref Next 1 30.000 16.80 92.02 92.02 5.41 2.635 10.000 2 30.346 16.80 92.54 184.56 10.86 2.635 9.000 0.0 10.000 100 0.0346 0.346 0.0 0.0 30.346'2 3 31.475 16.80 94.26 278.82 16.40 2.635 8.583 1 T 0.0 9.000 100 0.1254 1.129 0.0 0.0 31.475 3 100 36.946 45.87 0.0 278.82 11.757 20.340 100 0.2690 5.471 0.0 0.0 36.946 100 4 34.663 16.80 98.91 98.91 5.82 2.635 10.000 5 35.058 16.80 99.47 198.38 11.67 2.635 1.417 IT 1.0 13.174 100 0.0395 0.395 0.0 0.0 35.058 5 100 36.946 32.64 0.0 198.38 11.757 13.174 100 0.1433 1.888 0.0 0.0 36.946 100 6 30.069 16.80 92.12 92.12 5.42 2.635 10.000 7 30.416 16.80 92.66 184.78 10.87 2.635 9.000 0.0 10.000 100 0.0347 0.347 0.0 0.0 30.416 7 8 31.547 16.80 94.36 279.14 16.42 2.635 8.583 IT 110.757 20.340 100 0.2696 5.483 0.0 0.0 37.030 8 101 37.030 45.87 0.0 279.14 01 9 34.742 16.80 99.02 99.02 5.83 2.635 10.000 0.0 10.000 100 0.0396 0.396 0.0 0.0 35.138 10 10 35.138 16.80 99.59 198.61 11.69 2.635 1.417 IT 101 37.030 32.64 0.0 198.61 11.757 13.174 100 0.1436 1.892 0.0 0.0 37.030 101 11 30.319 16.80 92.51 92.51 5.44 2.635 10.000 0.0 10.000 100 0.0350 0.350 0.0 0.0 30.669 12 12 30.669 16.80 93.03 185.54 10.92 2.635 9.000 0.0 9.000 100 0.1266 1.139 0.0 0.0 31.808 13 13 31.808 16.80 94.75 280.29 16.49 2.635 8.583 IT 102 37.334 45.87 0.0 280.29 11.757 20.340 100 0.2717 5.526 0.0 0.0 37.334 102 14 35.028 16.80 99.43 99.43 5.85 2.635 10.000 15 35.428 16.80 99.99 199.42 11.73 2.635 1.417 IT 0.0 10.000 100 0.0400 0.400 0.0 0.0 35.428 15 102 37.334 32.64 0.0 199.42 11.757 13.174 100 0.1447 1.906 0.0 0.0 37.334 102 16 30.850 16.80 93.31 93.31 5.49 2.635 10.000 0.0 10.000 100 0.0356 0.356 0.0 0.0 31.206 17 17 31.206 16.80 93.85 187.16 11.01 2.635 9.000 18 32.364 16.80 95.58 282.74 16.63 2.635 8.583 1T 0•0 9.000 100 0.1287 1.158 0.0 0.0 32.364 18 103 37.979 45.88 0.0 282.74 11.757 20.340 100 0.2761 5.615 0.0 0.0 37.979 103 19 35.636 16.80 100.29 100.29 5.90 2.635 10.000 20 36.042 16.80 100.86 201.15 11.83 2.635 1.417 IT 0.0 10.000 100 0.0406 0.406 0.0 0.0 36.042 20 103 37.979 32.64 0.0 201.15 11.757 13.174 100 0.1470 1.937 0.0 0.0 37.979 103 21 31.760 16.80 94.68 94.68 5.57 2.635 10.000 22 32.125 16.80 95.22 189.9 11.17 2.635 9.000 0.0 10.000 100 0.0365 0.365 0.0 0.0 32.125 22 23 33.315 16.80 96.97 286.87 16.88 2.635 8.583 1 T 0.0 9.000 100 0.1322 1.190 0.0 0.0 33.315 23 104 39.082 45.89 0.0 286.87 11.757 20.340 100 0.2835 5.767 0.0 0.0 39.082 104 24 36.676 16.80 101.74 101.74 5.99 2.635 10.000 25 37.093 16.80 102.32 204.06 12.01 2.635 1.417 1 T 0.0 10.000 100 0.0417 0.417 0.0 0.0 37.093 25 104 39.082 32.64 0.0 204.06 11.757 13.174 100 0.1510 1.989 0.0 0.0 39.082 104 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line Page 6 SA Comunale Date 3.1.18 Quell System 3 Tot C Pf Tot Elev Fixed Next Next Ref Press K Flow Flow Pipe Pipe Fit Fit Pf Press Loss Press Ref Pt. Total Fact. Added Total Vel Diam. Length Sum. Length Len Fac perUL 100 36.946 477.20 477.2 18.34 3.26 2.000 IT 14.387 16.387 100 0.2579 4.226 0.0 0.0 41.172 200 200 41.172 74.37 0.0 477.20 101 37.030 477.75 477.75 18.36 3.26 2.000 IT 14.387 16.387 100 0.2584 4.235 0.0 0.0 41.265 201 201 41.265 74.37 0.0 477.75 2.000 1 T 14.387 16.387 100 0.2604 4.267 0.0 0.0 41.60'i 202 102 37.334 479.72 479.72 18.44 3.26 202 41.601 74.38 0.0 479.72 103 37.979 483.88 483.88 18.60 3.26 2.000 IT 14.387 16.387 100 0.2645 4.335 0.0 0.0 42.314 2 03 203 42.314 74.39 0.0 483.88 104 39.082 490.93 490.93 18.87 3.26 2.000 1 T 14.387 16.387 100 0.2717 4.453 0.0 0.0 43.535 204 204 43.535 74.40 0.0 490.93 0.0 9.333 100 0.0100 0.093 0.0 0.0 41.265 201 200 41.172 477.20 477.2 4.82 6.357 9.333 201 41.265 477.74 954.94 9.65 6.357 9.333 0.0 9.333 100 0.0360 0.336 0.0 0.0 41.601 202 202 41.601 479.72 1434.66 14.50 6.357 9.333 0.0 9.333 100 0.0764 0.713 0.0 0.0 43.535 203 203 42.314 483.89 1918.55 19.39 6.357 9.333 0.0 9.333 100 0.1308 1.221 0.0 0.0 43.535 204 04 24.36 6.357 102.667 0.0 102.667 100 0.1995 20.478 0.0 0.0 64.013 RDCR 2 43.535 490.92 2409.47 04 43.535 0.0 2409.47 2 4.46 8.249 129.000 5V 54.485 183.485 100 0.0561 10.291 0.0 0.0 74.304 300 300 74.304 279.52 0.0 2409.47 300 74.304 2409.47 2409.47 14.46 8.249 17.083 2V 21.794 38.877 100 0.0561 2.180 1.516 0.0 78.000 TOR TOR 78.000 272.82 0.0 2409.47 TOR 78.000 2409.47 2409.47 14.46 8.249 25.000 1S2B1T4# .87.176 112.176 100 0.0561 6.29114.292 4.000 102.583 BOR 2.583 0.0 2409.47 14.46 8.249 4.000 1 V 15.269 19.269 120 0.0400 0.771 0.0 0.0 103.354 RM2 BOR 10 0.0 2409.47 14.46 8.249 329.000 4V1U 66.947 395.947 120 0.0400 15.848 0.0 0.0 119.202 RM1 RM2 10 RM2 119.202 3.583 354 0.0 2409.47 11.09 9.42 280.000 5L1 F1 G 107.388 387.388 150 0.0139 5.376 0.0 0.0 124.578 UG UG 124.578 H500 500.00 2909.47 13.39 9.42 15.000 1 S1 B1 L 100.677 115.677 150 0.0197 2.275 0.0 0.0 126.853 PO PO 126.853 258.32 0.0 2909.47 Computer Programs by Hydratec Inc. Revision: 50.52 1 y ,J SA Comunale Page 1 Dry System 4 Date 3.1.18 HYDRAULIC CALCULATIONS for Project name: Aldi South Windsor Location: 295 Rye Street, South Windsor, CT Drawing no: 4 Date: 3.1.18 Design Remote area number: 4 Remote area location: 4 Occupancy classification: Ordinary Hazard 2 Density: .2 - Gpm/SgFt Area of application: 2600-SgFt Coverage per sprinkler: 120 -SgFt Type of sprinklers calculated: 8.Ok uprights No, of sprinklers calculated: 23 In-rack demand: -GPM Hose streams: 500-GPM Total water required(including hose streams): 1326.58 - GPM @ 140.59- Psi Type of system: Dry system Volume of dry or preaction system: 670- Gal Water supply information Date: Location: Fire Pump room Source: Name of contractor: SA Comunale Address: 2900 Newpark Drive/ /Barberton, OH 44203 Phone number: Name of designer: Authority having jurisdiction: Notes:(Include peaking information or gridded systems here.) 1\!lplStlCSil ti 1�'.1;it alll/f fi16 Af sl 1/1111/11 I!f i l lilt\ti\\\!\ Water Supply Curve C SA Comunale Page 2 Date 3.1.18 Dry System 4 Pump Data: Demand: P1 - Pump Churn Pressure 177 D1 - Elevation 9.9:61 P2 - Pump Rated Pressure 160 D2- System Flow : 826.58 P2 - Pump Rated Flow 2000 D2-System Pressure : 140.592 P3 - Pump Pressure @ Max Flow 120 Hose ( Demand ) : 500 P3 - Pump Max Flow 3750 Safety 58 s System Demand : 123�26 717 180 168 156 P 144 R 132 D3 P3 E 120 S 108 S 96 U 84 R 72 E 60 48 36 24 12 D1 400 800 1200 1600 2000 2400 2800 3200 3600 FLOW ( N^1.85 ) Comp iter PYnnamE h4 H irat c Inc. Re v-'�� n: 5n.52 1 Fittings Used Summary SA Comunale Dry System 4 Page 3 Date 3.1.18 Fitting Legend Abbrev. Name Y2 3/4 1 1'/4 1Y2 2 2Y2 3 3Y2 4 5 6 8 10 12 14 16 18 20 24 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 Dvc Dry Vic 768 NXT 3 9 8 17 21 22 50 F NFPA 13 45'Elbow 1 1 1 1 2 2 3 3 3 4 5 7 9 11 13 17 19 21 24 28 G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 L NFPA 13 Long Turn Elbow 0.5 1 2 2 2 3 4 5 5 6 8 9 13 16 18 24 27 30 34 40 S NFPA 13 Swing Check 0 0 5 7 9 11 14 16 19 22 27 32 45 55 65 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 V 90'Ell Firelock#001 0 0 0 0 0 3.5 4.3 5 0 6.8 8.5 10 13 4.5 5.1 0 0 0 0 0 X 90'Tee-BranchFirelock002 0 0 0 0 0 8.5 10.8 13 0 16 21 25 33 9.3 11 0 0 0 0 0 Unit Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *. The fittings marked with a*show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a*will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Revision: 50.52.1 Pressure / Flow Summary - STANDARD SA Comunale Page 4 Dry System 4 Date 3.1.18 Node Elevation K-Fact Pt Pn Flow Density Area Press No Actual Actual ___ Reg. 1 25.0 8 9.0 na 24.0 0.2 120 7.0 2 25.0 8 9.26 na 24.35 0.2 120 7.0 3 25.0 8 10.22 na 25.58 0.2 120 7.0 4 25.0 8 12.33 na 28.09 0.2 120 7.0 5 25.0 8 16.16 na 32.16 0.2 120 7.0 6 25.0 8 22.51 na 37.95 0.2 120 7.0 7 25.0 8 32.57 na 45.66 0.2 120 7.0 8 25.0 8 52.4 na 57.91 0.2 120 7.0 9 25.0 8 9.05 na 24.06 0.2 120 7.0 10 25.0 8 9.31 na 24.41 0.2 120 7.0 11 25.0 8 10.28 na 25.65 0.2 120 7.0 12 25.0 8 12.4 na 28.17 0.2 120 7.0 13 25.0 8 16.24 na 32.24 0.2 120 7.0 14 25.0 8 22.62 na 38.05 0.2 120 7.0 15 25.0 8 32.74 na 45.77 0.2 120 7.0 16 25.0 8 52.66 na 58.05 0.2 120 7.0 17 25.0 8 14.26 na 30.21 0.2 120 TO 18 25.0 8 14.67 na 30.64 0.2 120 7.0 19 25.0 8 16.14 na 32.14 0.2 120 7.0 20 25.0 8 19.36 na 35.2 0.2 120 7.0 21 25.0 8 25.19 na 40.15 0.2 120 7.0 22 25.0 8 34.85 na 47.23 0.2 120 7.0 23 25.0 8 54.24 na 58.92 0.2 120 7.0 50 38.5 41.91 na 51 38.5 48.18 na 52 38.5 49.79 na 60 38.5 70.29 na 61 38.5 70.66 na 62 38.5 71.99 na l 63 38.5 77.09 na TDR 35.0 124.26 na BDR 2.0 139.42 na RM1 2.0 139.52 na UG 2.0 140.06 na 500.0 I PO 2.0 140.59 na ill The maximum velocity is 43.56 and it occurs in the pipe between nodes 51 and 61 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line SA Comunale Page 5 x Dry System 4 Date 3.1.18 Ref Press K Flow Flow Pipe Pipe Fit Fit Tot C Pf Tot Elev Fixed Next Next Pt. Total Fact. Added Total Vel Diam. Length Sum. Length Len Fac perUL Pf Press Loss Press Ref 1 9.000 8.00 24.00 24.0 3.78 1.61 8.292 0.0 8.292 100 0.0317 0.263 0.0 0.0 9.263 2 2 9.263 8.00 24.35 48.35 7.62 1.61 8.292 0.0 8.292 100 0.1159 0.961 0.0 0.0 10.224 3 3 10.224 8.00 25.58 73.93 11.65 1.61 8.292 0.0 8.292 100 0.2542 2.108 0.0 0.0 12.332 4 4 12.332 8.00 28.09 102.02 16.08 1.61 8.292 0.0 8.292 100 0.4613 3.825 0.0 0.0 16.157 5 5 16.157 8.00 32.16 134.18 21.15 1.61 8.292 0.0 8.292 100 0.7658 6.350 0.0 0.0 22.507 6 6 22.507 8.00 37.95 172.13 27.13 1.61 8.292 0.0 8.292 100 1.2141 10.067 0.0 0.0 32.574 7 7 32.574 8.00 45.66 217.79 34.32 1.61 5.583 1 T 5.71 11.293 100 1.8761 21.187-5.847 0.0 47.914 50 50 47.914 31.46 0.0 217.79 8 52.399 8.00 57.91 57.91 9.13 1.61 2.708 1 T 5.71 8.418 100 0.1618 1.362-5.847 0.0 47.914 50 50 47.914 8.37 0.0 57.91 9 9.048 8.00 24.06 24.06 3.79 1.61 8.292 0.0 8.292 100 0.0318 0.264 0.0 0.0 9.312 10 10 9.312 8.00 24.42 48.48 7.64 1.61 8.292 0.0 8.292 100 0.1165 0.966 0.0 0.0 10.278 11 11 10.278 8.00 25.64 74.12 11.68 1.61 8.292 0.0 8.292 100 0.2554 2.118 0.0 0.0 12.396 12 12 12.396 8.00 28.17 102.29 16.12 1.61 8.292 0.0 8.292 100 0.4636 3.844 0.0 0.0 16.240 13 13 16.240 8.00 32.24 134.53 21.20 1.61 8.292 0.0 8.292 100 0.7694 6.380 0.0 0.0 22.620 14 14 22.620 8.00 38.05 172.58 27.20 1.61 8.292 0.0 8.292 100 1.2199 10.115 0.0 0.0 32.735 15 15 32.735 8.00 45.77 218.35 34.41 1.61 5.583 1 T 5.71 11.293 100 1.8851 21.288-5.847 0.0 48.176 51 51 48.176 31.46 0.0 218.35 16 52.655 8.00 58.05 58.05 9.15 1.61 2.708 1 T 5.71 8.418 100 0.1625 1.368-5.847 0.0 48.176 51 51 48.176 8.36 0.0 58.05 17 14.263 8.00 30.21 30.21 4.76 1.61 8.292 0.0 8.292 100 0.0485 0.402 0.0 0.0 14.665 18 18 14.665 8.00 30.64 60.85 9.59 1.61 8.292 0.0 8.292 100 0.1774 1.471 0.0 0.0 16.136 19 19 16.136 8.00 32.13 92.98 14.65 1.61 8.292 0.0 8.292 100 0.3886 3.222 0.0 0.0 19.358 20 20 19.358 8.00 35.20 128.18 ' 20.20 1.61 8.292 0.0 8.292 100 0.7037 5.835 0.0 0.0 25.193 21 21 25.193 8.00 40.16 168.34 26.53 1.61 8.292 0.0 8.292 100 1.1650 9.660 0.0 0.0 34.853 22 22 34.853 8.00 47.23 215.57 33.97 1.61 5.583 1 T 5.71 11.293 100 1.8409 20.789-5.847 0.0 49.795 52 52 49.795 30.55 0.0 215.57 23 54.236 8.00 58.92 58.92 9.29 1.61 2.708 1 T 5.71 8.418 100 0.1670 1.406-5.847 0.0 49.795 52 52 49.795 8.35 0.0 58.92 50 47.914 275.70 275.7 43.45 1.61 2.000 1 T 5.71 7.710 100 2.9019 22.374 0.0 0.0 70.288 60 60 70.288 32.88 0.0 275.70 51 48.176 276.40 276.4 43.56 1.61 2.000 1 T 5.71 7.710 100 2.9157 22.480 0.0 0.0 70.656 61 61 70.656 32.88 0.0 276.40 52 49.795 274.48 274.48 43.26 1.61 2.000 1 T 5.71 7.710 100 2.8783 22.192 0.0 0.0 71.987 62 62 71.987 32.35 0.0 274.48 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - One-Line SA Comunale Page 6 Dry System 4 Date 3.1.18 Ref Press K Flow Flow Pipe Pipe Fit Fit Tot C Pf Tot Elev Fixed Next Next Pt. Total Fact. Added Total Vel Diam. Length Sum. Length Len Fac perUL Pf Press Loss Press Ref 60 70.288 275.70 275.7 6.21 4.26 14.500 0.0 14.500 100 0.0254 0.368 0.0 0.0 70.656 61 61 70.656 276.40 552.1 12.43 4.26 14.500 0.0 14.500 100 0.0918 1.331 0.0 0.0 71.987 62 62 71.987 274.48 826.58 18.61 4.26 11.333 ix 15.035 26.368 100 0.1936 5.105 0.0 0.0 77.092 63 63 77.092 0.0 826.58 18.61 4.26 216.667 3V 19.17 235.837 100 0.1936 45.656 1.516 0.0 124.264 TDR TDR 124.264 74.15 0.0 826.58 TDR 124.264 826.58 826.58 4.96 8.249 30.000 1B1T1Dvc 81.308 111.308 100 0.0078 0.86314.292 0.0 139.419 BDR BDR 139.419 0.0 826.58 4.96 8.249 4.000 1L 15.269 19.269 120 0.0055 0.106 0.0 0.0 139.525 RM1 RM 1 139.525 0.0 826.58 3.11 10.42 280.000 5L1 F1 G 175.527 455.527 150 0.0012 0.535 0.0 0.0 140.060 UG UG 140.060 H500 500.00 1326.58 6.11 9.42 15.000 1 S1 B1 L 100.677 115.677 150 0.0046 0.532 0.0 0.0 140.592 PO PO 140.592111.88 0.0 1326.58 a Y; Commuter PrograMF h`,'l-1"rlrpt,�r. Inr. R-vi5inn- FO F? 1 CALCULATION SUMMARY s• Project Name:Aldi South Windsor Project Location: 295 Rye Street Drawing No. : City: South Windsor, CT Headsets Headset Calculated Trip Time Transit Calc. Required Max. Pump Accelerator DPV Open Exhausters Name Time Time Delivery Delivery Operating Activation Used Tripped By Heads Time Time Time Time (s) (s) (s) (s) (s) (s) # # Headset-1 Operating 4.02 20.18 24.2 N/A 24.258 N/A Yes DPV Acc. 4 `44 Yad/rk CD US G3: QVIEm4) cot '�'�jOJ>I,yA5.7iFdi89di�[t5\\t��� Date 3/2/2018 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Copyright©2002-2012 Tyco Fire Protection Products Page 1 Node Labels: Off Job:Aldi South Windsor Pipe Labels: Off Diagram for Headset : Headset-1 File:VANorton Drawings\09 Brian.M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 2 i r Job :Aldi South Windsor i Time Analysis for : Headset 1 Dry pipe system System Volume 2640.4 gal Downstream DPV Volume 1942 gal Fluid Water @ 60F(15.6C) Gas Air @ 39.9°F and 50psi Differential Trip Ratio 0 (Deluge valve) Accelerator Differential Presure: Opsi Time Delay: 4s Headset Time Parameters Trip Time 4.02s Fluid Delivery Time 24.2s @ h224 Operating Time 24.258s @ h224 Required Fluid Delivery Time N/A Safety Factor N/A Water Supply Parameters Flow (gpm) Pressure (psi) 0 177 1000 174 2000 160 2900 150 3000 140 3750 120 Parameters of the 4 Open Heads Head# K-Factor Orifice Minimum Transit Time Fluid Oper.Time Open Time Operating Delivery SHALL NOT Pressure Time exceed N/A (9Pm/Psi'/2) (in) (Psi) (s) (s) (s) (s) h222 16.8 0.772 30 20.03 24.05 24.058 3 h224 16.8 0.772 30 20.18 24.2 24.258 5 h101 16.8 0.772 30 19.7 23.72 24.058 7 h107 16.8 0.772 30 19.89 23.91 24.258 0 Protocol: NOT USED NOT USED Statement Modelling Assumptions I. Fluid is incompressible. 2. Pipes do not suffer deformation. 3. Fluid front is perpendicular to pipe centerline. 4.The dry pipe valve opens instantly. File:V:\Norton Drawings\09 Brian M\Brian's DrawingsW cli South Windsor\CALCS\trip caics\sys i.tyc3 Date 3/2/2018 Copyright @ 2002-2012 Tyco Fire Protection Products Page 3 h222 — Pressure, psi — Flow, gpm -220 150 . 00 140 2 130 - _ 180 120 a. 160 110 100 140 _n a 90 120 80 _ 100 3 70 80 a 60 H 50 L. 40 M 60 30 h.>. 40 20 3 " 20 10 r , i s -10 ,n a n 1-20 0 5 10 15 20 25 30 35 Time, s h224 — Pressure, psi — Flow, gpm 160 -220 200 140 m - 180 120 160 100 xr, 140 120 80 100 °- 60 -80 40 '"� 6 0 -40 20 „ 20 j -20 0 5 10 15 20 25 30 35 Time, s File:V:Worton Drawings\09 Brian M\Brian's Drawings\Nldi South Windsor\CALCS\trip calcs\sys 1 tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 4 DPV (n95) — Pressure, psi — Flow, gpm I 180 _ 4,500 160. 4,000 140 ..3,500 a 120 3,000 100 0 T 2,500 ;v 80 _ 2,000 3 60 1,500 40 „ . o .-. 1,000 20 _.. . .._ ._.. 500 0 0 0 5 i0 15 2°0 25 30 35 Time, s srcl Pressure, psi — Flow, gpm 1804 500 _. <.. , 160 .... ...., .M 4,000 14000 3 5 120 CI -3,000 100 2,500 u80 _.. ... . .. ....... . 3 60 1,500 40 Fv. " - 1,000 20 500 0 _. :.. 0 0 5 10 15 20 25 30 35 Time, s Date 3/2/2018 File:V:\Norton Drawings\Og Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip caics\sys 1.tyc3 Copyright©2002-2012 Tyco Fire Protection Products Page 5 h101 — Pressure, psi — Flow, gpm 220 140 200 - 180 120 160 140 100 -^ CL 120 N80 w W 100 a 60 _ 80 ..... - .F 60 40 _. 40 . 20 20 B -20 0 5 10 15 20 25 30 35 Time, s h107 — Pressure, psi — Flow, gpm 160 M.... . 220 f 200 140 180 120 160 140 100 - ° 120 80 in M 100 9 L 60 R.Po b 80 60 40 20 20 , 0 0- -20 0 5 10 15 20 25 30 35 Time, s File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip caics\sys 1 tyc3 Page 6 Date 3/2/2018 Copyright 0 2002-2012 Tyco Fire Protection Products Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/Psi'/2 ft ft psi ft2 ft h109 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 1 h113 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 1 h6 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 1 n112 NODE -91.5 Node us.Tee 0 39 1 n130 NODE -91.5 Node us.Tee 0 37 1 h114 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 10.58 h118 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 10.58 h12 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 10.58 n113 NODE -91.5 Node us.Tee 0 39 10.58 n131 NODE 37 -91.5 Node us.Tee 0 10.58 11119 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 20.17 h123 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 20.17 h18 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 20.17 n114 NODE 39 -91.5 Node us.Tee 10 20.17 n132 NODE -91.5 Node us.Tee 0 37 20.17 11124 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 29.75 11128 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 29.75 h24 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 29.75 n115 NODE 39 -91.5 Node us.Tee 0 29.75 n133 NODE -91.5 Node us.Tee 0 37 29.75 h129 HEAD 16.8 39 115.25 Overhead Sprinkler 0 91.04 39.33 h133 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 39.33 1130 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 39.33 n116 NODE -91.5 Node us.Tee 10 39 39.33 n134 NODE 37 -91.5 Node us.Tee 0 39.33 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright @ 2002-2012 Tyco Fire Protection Products Page 7 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/psis/2 ft ft psi ft2 ft h134 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 48.92 h138 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 48.92 h200 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 173.49 n117 NODE 39 -91.5 Node us.Tee 10 48.92 n135 NODE 37 -91.5 Node us.Tee 0 48.92 h139 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 58.5 h143 HEAD 16.8 39 -77.25 Overhead Sprinkler 10 91.04 58.5 h202 HEAD 16.8 39 -23.58 Overhead Sprinkler0 __ 91.04-. . 183.08 n118 NODE 39 -91.5 Node us.Tee 0 58.5 n136 NODE 37 -91.5 Node us.Tee 0 58.5 h144 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 68.08 h148 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 68.08 h204 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 192.66 n119 NODE 39 -91.5 Node us.Tee 0 68.08 n137 NODE 37 -91.5 Node us.Tee 10 68.08 h149 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 77.66 h153 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 77.66 h206 HEAD 16.8 39 -23.58 Overhead Sprinkler 10 91.04 202.24 n120 NODE 39 -91.5 Node us.Tee 0 77.66 n138 NODE -91.5 Node us.Tee 0 37 77.66 h154 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 87.25 h158 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 87.25 h208 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 211.83 n121 NODE 39 -91.5 Node us.Tee 0 87.25 n139 NODE 37 -91.5 Node us.Tee 0 87.25 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright®2002-2012 Tyco Fire Protection Products Page 8 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/psi'/2 It ft psi ft2 ft h159 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 96.83 h163 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 96.83 h210 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 221.41 n122 NODE 39 -91.5 Node us.Tee 0 96.83 n140 NODE 37 -91.5 Node us.Tee 0 96.83 h164 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 106.41 h168 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 106.41 h212 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 230.99 n123 NODE 39 -91.5 Node us.Tee 0 106.41 n141 NODE 37 -91.5 Node us.Tee 0 106.41 h169 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 116 h173 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 116 h214 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 240.58 n124 NODE 39 -91.5 Node us.Tee 0 116 n142 NODE -91.5 Node us.Tee 0 37 116 h174 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 125.58 h178 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 125.58 h216 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 250.16 n125 NODE 39 -91.5 Node us.Tee 0 125.58 n143 NODE 37 -91.5 Node us.Tee 0 125.58 h179 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 135.16 h183 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 135.16 h218 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 259.74 n126 NODE -91.5 Node us.Tee 0 39 135.16 n144 NODE 37 -91.5 Node us.Tee 0 135.16 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 9 Job:Aidi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/psis/2 ft ft psi ft2 ft h184 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 144.75 h188 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 144.75 h220 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 269.32 n127 NODE 39 -91.5 Node us.Tee 10 144.75 n145 NODE 37 -91.5 Node us.Tee 0 144.75 h189 HEAD 16.8 39 -115.25 Overhead Sprinkler 0 91.04 154.33 h193 16.8 39 -77.25 Overhead Sprinkler HEAD 0 91.04 154.33 h222 HEAD 16.8 39 -23.58 Overhead.Sprinkler . 0- _ 91.04. . 278..91 n128 NODE 39 -91.5 Node us.Tee 0 154.33 n146 NODE 37 -91.5 Node us.Tee 0 154.33 1 h194 HEAD 16.8 39 -115.25 11 Overhead Sprinkler 0 91.04 163.91 h198 HEAD 16.8 39 -77.25 Overhead Sprinkler 0 91.04 163.91 . h224 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 288.49 n129 NODE 1 39 -91.5 Node us.Tee 0 163.91 n36 NODE 37 -91.5 Node us.90 0 163.91 n92 NODE 37 -115.25 Node us.90 0 -69 n93 NODE 8 -115.25 Node coupling 0 -69 n94 NODE 7 -115.25 Node coupling 0 -69 n95 NODE 6 -115.25 Node coupling 0 -69 n96 NODE 5 -115.25 Node coupling 0 -69 n97 NODE 4 -115.25 Node us.90 0 -69 n98 NODE 4 -115.25 Node us.90 0 -74 n101 NODE _1 -115.25 Node us.90 0 -84 n102 NODE _1 -172.25 Node BM.90 0 -84 n103 NODE _1 -172.25 Node BM.90 0 -199 File:V:Worton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip caics\sys 1.tyc3 Date 3/2/2018 Copyright 0 2002-2012 Tyco Fire Protection Products Page 10 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/psiY2 ft ft psi ft2 ft n104 NODE -135.25 Node BM.90 0 -1 -199 n105 NODE -135.25 Node BM.90 0 -1 -250 n106 NODE -125.25 Node BM.90 0 -1 -250 n107 NODE -125.25 Node us.90 0 4 -250 srcl SUPPLY 4 -115.25 Supply 0 -250 n108 NODE -115.25 Node us.90 0 -1 -74 n109 NODE -115.25 Node us.90 0 37 -1 n148 NODE 37 -91.5 Node us.Tee 0 -1 h1 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 1 n1 NODE -47.33 Node us.Tee 0 39 1 h7 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 10.58 n3 NODE -47.33 Node us.Tee 0 39 10.58 h13 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 20.17 n5 NODE -47.33 Node us.Tee 0 39 20.17 h19 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 29.75 n7 NODE 39 -47.33 Node us.Tee 0 29.75 h25 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 39.33 n9 NODE 39 -47.33 Node us.Tee 0 39.33 h225 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 173.49 n149 NODE 39 -47.33 Node us.Tee 0 173.49 h229 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 183.08 n151 NODE 39 -47.33 Node us.Tee 10 183.08 11233 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 192.66 n153 NODE 39 -47.33 Node us.Tee 0 192.66 h237 HEAD 16.8 39 -71.08 Overhead Sprinkler 1 10 91.04 202.24 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip caics\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 11 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/psis/z ft ft psi ftZ ft n155 NODE 39 -47.33 Node us.Tee 0 202.24 h241 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 211.83 niS7 NODE 39 -47.33 Node us.Tee 0 211.83 h245 HEAD 16.8 39 -71.08 Overhead Sprinkler 10 91.04 221.41 n159 NODE 39 -47.33 Node us.Tee 0 221.41 h249 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 230.99 n161 NODE 39 -47.33 Node I us.Tee 10 230.99 h253 HEAD 16.8 39 -71.08 Overhead Sprinkler _ 0____. __ _91,04 240.58. n163 NODE 39 -47.33 Node us.Tee 0 240.58 h257 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 250.16 n165 NODE 39 -47.33 Node us.Tee 0 250.16 h261 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 259.74 n167 NODE 39 -47.33 Node us.Tee 0 259.74 h265 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 269.32 n169 NODE 39 -47.33 Node us.Tee 0 269.32 h269 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 278.91 n171 NODE 39 -47.33 Node us.Tee 0 278.91 h101 HEAD 16.8 39 -33.08 Overhead Sprinkler 0 91.04 278.91 h273 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 288.49 n173 NODE 39 -47.33 Node us.Tee 0 288.49 h107 HEAD 16.8 39 -33.08 Overhead Sprinkler 0 91.04 288.49 n2 NODE 37 -47.33 Node us.Tee 0 1 n4 NODE 37 -47.33 Node us.Tee 0 10.58 n6 NODE 37 -47.33 Node us.Tee 0 20.17 n8 NODE 37 -47.33 Node us.Tee 0 29.75 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright®2002-2012 Tyco Fire Protection Products Page 12 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/psi'/z ft ft psi ftz ft n 150 NODE -47.33 Node us.Tee 0 37 173.49 n 152 NODE -47.33 Node us.Tee 0 37 183.08 n 154 NODE -47.33 Node us.Tee 0 37 192.66 n 156 NODE -47.33 Node us.Tee 0 37 202.24 n158 NODE -47.33 Node us.Tee 0 37 211.83 n160 NODE -47.33 Node us.Tee 0 37 221.41 n 162 NODE -47.33 Node us.Tee 10 37 230.99 n 164 NODE -47.33 Node us.Tee 0 37 240.58 n166 NODE -47.33 Node us.Tee 0 37 250.16 n 168 NODE -47.33 Node us.Tee 10 37 259.74 n 170 NODE -47.33 Node us.Tee 0 37 269.32 n172 NODE -47.33 Node us.Tee 0 37 278.91 n 175 NODE -47.33 Node us.90 0 37 288.49 n 110 NODE -47.33 Node us.90 0 37 -1 h36 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 48.92 h42 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 58.5 1148 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 68.08 h54 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 77.66 h60 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 87.25 h66 HEAD 16.8 39 -23.58 Overhead Sprinkler 10 91.04 96.83 h72 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 106.41 h78 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 116 h84 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 125.58 1190 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 135.16 1196 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 1144.75 File:V:\Norton Drawingsk09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 13 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev_ X Type Fitting Stat. Pres. Coverage Y gpm/psis/2 ft ft psi ft2 ft h102 HEAD 16.8 39 -23.58 Overhead Sprinkler 10 91.04 154.33 h108 HEAD 16.8 39 -23.58 Overhead Sprinkler 0 91.04 163.91 h31 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 48.92 n1I NODE 39 -47.33 Node us.Tee 10 48.92 n12 NODE 37 -47.33 Node us.Tee 0 48.92 h37 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 58.5 n13 NODE 39 -47.33 Node us.Tee 0 58.5 n14 NODE 37 -47.33 Node. ___ us.Tee_. 0_._ _ _ _ . 58.5___, _. h43 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 68.08 n15 NODE 39 -47.33 Node us.Tee 10 68.08 n16 NODE 37 -47.33 Node us.Tee 0 68.08 h49 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 77.66 n17 NODE 39 -47.33 Node us.Tee 10 77.66 n18 NODE 37 -47.33 Node us.Tee 0 77.66 h55 16.8 39 -71.08 Overhead Sprinkler HEAD 0 91.04 87.25 n19 NODE 39 -47.33 Node us.Tee 0 87.25 n20 NODE 37 -47.33 Node us.Tee 0 87.25 h61 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 96.83 n21 NODE 39 -47.33 Node us.Tee 0 96.83 n22 NODE 37 -47.33 Node us.Tee 0 96.83 h67 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 106.41 n23 NODE 39 -47.33 Node us.Tee 0 106.41 n24 NODE 37 -47.33 Node us.Tee 0 106.41 h73 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 116 n25 NODE 39 -47.33 Node us.Tee 0 116 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 14 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Hgroup K-Fact. Elev X Type Fitting Stat. Pres. Coverage Y gpm/Psi'/2 ft ft psi ftz ft n26 NODE -47.33 Node us.Tee 0 37 116 h79 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 125.58 n27 NODE -47.33 Node us.Tee 0 39 125.58 n28 NODE -47.33 Node us.Tee 0 37 125.58 h85 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 135.16 n29 NODE -47.33 Node us.Tee 0 39 135.16 n30 NODE -47.33 Node us.Tee 0 37 135.16 h91 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 144.75 n31 NODE -47.33 Node us.Tee 0 39 144.75 n32 NODE 37 -47.33 Node us.Tee 0 144.75 h97 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 154.33 n33 NODE -47.33 Node us.Tee 0 39 154.33 n34 NODE -47.33 Node us.Tee 0 37 154.33 h103 HEAD 16.8 39 -71.08 Overhead Sprinkler 0 91.04 163.91 n35 NODE -47.33 Node us.Tee 0 39 163.91 n174 NODE 37 -47.33 Node us.Tee 0 163.91 n147 NODE -47.33 Node us.Tee 0 37 39.33 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 15 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Pipe Data Pipe Ref. Type Start End Schedule Size Length Fittings Eq.Len. Total Len. ft ft It rn18 Rnppl n174 n35 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b106 Brline n35 h108 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b105 Brline n35 h103 1OGaly 2.5 123.75 1(us.Tee-Br); 16.47 40.22 m17 Cmain n34 n174 1OGaly 6 9.58 1(us.Tee-Run); rn17 Rnppl n34 n33 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 MOO Brline n33 h102 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b99 Brline n33 h97 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 140.22 m16 Cmain n32 n34 10Galy 6 19.58 1(us.Tee-Run); rn16 Rnppl n32 n31 1OGaly 3 12 1(us.Tee-Br); 20.16 22.16 b94 Brline n31 h96 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b93 Brline n31 h91 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 m15 Cmain n30 n32 1OGaly 6 9.58 1(us.Tee-Run); rn15 Rnppl n30 n29 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b88 Brline n29 h90 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 . b87_ ___ Brline- n2.9_ -h8-5 1OGaly--- 2.5 - 23.75 1(us.Tee-Br);-_. 16.47_ 40.22--._ m14 Cmain n28 n30 1OGaly 6 9.58 1(us.Tee-Run); rn14 Rnppl n28 n27 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b82 Briine n27 h84 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b81 Brline n27 h79 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 m13 Cmain n26 n28 1OGaly 6 9.58 1(us.Tee-Run); rn13 Rnppl n26 n25 1OGaly 13 12 11(us.Tee-Br); 20.16 22.16 b76 Brline n25 h78 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b75 Brline n25 h73 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 m12 Cmain n24 n26 1OGaly 6 9.58 1(us.Tee-Run); rn12 Rnppl n24 n23 IOGaly 3 2 1(us.Tee-Br); 20.16 22.16 b70 Brline n23 h72 10Galy 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b69 Brline n23 h67 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 m11 Cmain n22 n24 IOGaly 6 9.58 1(us.Tee-Run); rn11 Rnppl n22 n21 IOGaly 3 2 1(us.Tee-Br); 20.16 22.16 b64 Brline n21 h66 IOGaly 2.5 123.75 1(us.Tee-Br); 16.47 40.22 b63 Brline n21 h61 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 m10 Cmain n20 n22 1OGaly 6 9.58 1(us.Tee-Run); rn10 Rnppl n20 n19 IOGaly 3 2 1(us.Tee-Br); 20.16 22.16 b58 Brline n19 h60 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b57 Brline n19 h55 10Galy 2.5 123.75 1(us.Tee-Br); 16.47 140.22 m9 Cmain n18 n20 1OGaly 6 9.58 1(us.Tee-Run); rn9 Rnppl n18 n17 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b52 Brline n17 I h54 10Galy 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b51 Brline n17 h49 IOGaly 2.5 23.75 11(us.Tee-Br); 16.47 40.22 m8 Cmain n16 n18 1OGaly 6 9.58 1(us.Tee-Run); rn8 Rnppl n16 n15 10Galy 3 2 1(us.Tee-Br); 20.16 22.16 b46 Brline n15 h48 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b45 Brline n15 h43 IOGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 m7 j Cmain n14 n16 1OGaly 6 9.58 1 1(us.Tee-Run); File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright 0 2002-2012 Tyco Fire Protection Products Page 16 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Pipe Data Pipe Ref. Type Start End Schedule Size Length Fittings Eq.Len. Total Len. ft ft ft rn7 Rnppl n14 n13 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b40 Brline n13 h42 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b39 Brline n13 h37 1OGaly 2.5 123.75 1(us.Tee-Br); 16.47 140.22 m6 Cmain n12 n14 1OGaly 6 9.58 l(us.Tee-Run); m5 Cmain n147 n12 1OGaly 6 9.58 l(us.Tee-Run); rn6 Rnppl n12 nll 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b34 Brline n11 h36 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b33 Brline n11 1131 1OGaly 2.5 123.75 1 1(us.Tee-Br); 16.47 140.22 m47 Cmain n1721 n175 1OGaly 6 9.58 1 l(us.Tee-Run); m46 Cmain n1701 n172 1OGaly 6 9.58 1(us.Tee-Run); m45 Cmain n168 n170 1OGaly 6 9.58 1(us.Tee-Run); m44 Cmain n166 n168 1OGaly 6 9.58 l(us.Tee-Run); m43 Cmain n164 n166 1OGaly 6 19.58 l(us.Tee-Run); m42 Cmain n162 n164 1OGaly 6 9.58 l(us.Tee-Run); m41 Cmain n1601 n162 1OGaly 6 9.58 l(us.Tee-Run); m40 Cmain n1581 n160 lOGaly 6 9.58 l(us.Tee-Run); m39 Cmain n1561 n158 1OGaly - 6 9.58 l(us.Tee-Run); m38 Cmain n1541 n156 1OGaly 6 19.58 l(us.Tee-Run); m37 Cmain n152 n154 1OGaly 6 9.58 l(us.Tee-Run); m36 Cmain n150 n152 10Galy 6 9.58 l(us.Tee-Run); m35 Cmain n174 n150 1OGaly 6 9.58 l(us.Tee-Run); m4 Cmain n8 n147 10Galy 6 9.58 l(us.Tee-Run); m3 Cmain n6 n8 1OGaly 8 19.58 l(us.Tee-Run); m2 Cmain n4 n6 1OGaly 8 9.58 l(us.Tee-Run); fd2 FeedMain n110 n2 10Galy 8 2 1(us.90); 20.98 22.98 mi Cmain n2 n4 1OGaly 8 9.58 l(us.Tee-Run); rn49 Rnppl n175 n173 1OGaly 3 2 1(us.90); 9.41 11.41 b276 Byline n173 h107 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b275 Brline n173 h273 lOGaly 2.5 123.75 1(us.Tee-Br); 16.47 40.22 rn48 Rnppl n172 n171 lOGaly 3 2 1(us.Tee-Br); 20.16 22.16 b272 Brline n171 h101 I lOGaly 2.5 14.25 1(us.Tee-Br); 16.47 30.72 b271 Brline n171 11269 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 rn47 Rnppl n170 n169 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b268 Brline n169 h220 10Galy 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b267 Brline n169 h265 lOGaly 2.5 123.75 1(us.Tee-Br); 16.47 40.22 rn46 Rnppl n168 n167 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b264 Brline n167 h218 10Galy 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b263 Brline n167 h261 I SOGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 rn45 Rnppl n166 n165 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b260 Brline n165 11216 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b259 Brline n165 h257 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 rn44 Rnppl n164 n163 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b256 Brline n163 h214 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b255 Brline n163 h253 10Galy 2.5 23.75 1(us.Tee-Br); 16.47 140.22 File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 17 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Pipe Data Pipe Ref. Type Start End Schedule Size Length Fittings Eq.Len. Total Len. ft ft ft rn43 Rnppl n162 n161 10Galy 3 2 l(us.Tee-Br); 20.16 22.16 b252 Brline n161 h212 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b251 Brline n1611 h249 1OGaly 2.5 123.75 l(us.Tee-Br); 16.47 40.22 rn42 Rnppl n160 n159 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b248 Brline n159 h210 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b247 Brline n159 h245 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 rn41 Rnppl n158 n1571 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b244 Brline n157 h208 10Galy 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b243 Brline n157 h241 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 rn40 Rnppl n156 n155 lOGaly 3 2 l(us.Tee-Br); 20.16 22.16 b240 Brline n155 h206 lOGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b239 Brline n1551 h237 1OGaly 2.5 123.75 1 1(us.Tee-Br); 16.47 40.22 rn39 Rnppl n154 n153 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b236 Brline n153 11204 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b235 _ Brline- n153 h2-33 10Ga+v 2.5- 23.75- 1(us.Tee-Br); 16.47 40,Z2-.____ rn38 Rnppl n152 n1511 lOGaly 3 2 l(us.Tee-Br); 20.16 22.16 b232 Brline n151 h202 1OGaly 2.5 123.75 1 l(us.Tee-Br); 16.47 40.22 b231 Brline n151 11229 1OGaly 2.5 123.75 11(us.Tee-Br); 16.47 40.22 rn37 Rnppl n150 n149 10Galy 3 2 l(us.Tee-Br); 20.16 22.16 b228 Brline n149 h200 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b227 Brline n149 h2251 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 rn5 Rnppl n1471 n9 I 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b28 Brline n9 h30 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b27 Brline n9 1125 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 rn4 Rnppl n8 n7 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b22 Brline n7 h24 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b21 Brline n7 Ih19 I 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 rn3 Rnppl n6 In5 I 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b16 Brline n5 h18 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b15 Brline n5 h13 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 rn2 Rnppl n4 n3 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b10 Brline n3 1112 10Galy 2.5 123.75 l(us.Tee-Br); 16.47 40.22 b9 Brline n3 1117 1 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 rnl Rnppl n2 nl 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 b4 Brline nl h6 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b3 Brline n1 hl 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 140.22 FM4 Feed n148 n110 1OGaly 8 144.17 1 l(us.Tee-Run); FM3 Feed n1091 n148 10Galy 8 123.75 1(us.90); 20.98 44.73 FM2 Feed n92 I n109 lOGaly 8 168 1(us.90); 20.98 88.98 U10 Undergrnd n101 n108 DI350 10 10 1(us.90); 35.98 45.98 FM1 Feed srcl I n107 10 10 10 U9 Undergrnd n107 n106 PVC200 10 5 1(us.90); 24.31 29.31 U8 Undergrnd n106 n105 PVC200 10 10 U7 Undergrnd n105 n104 PVC200 10 151 File:V:\Norton Drawings\09 Brian N1\Brian's Drawings\Aidi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 18 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Pipe Data Pipe Ref. Type Start End Schedule Size Length Fittings Eq.Len. Total Len. ft ft ft U6 Undergrnd n104 n103 PVC200 10 37 U5 Undergrnd n103 n102 PVC200 10 115 U4 Undergrnd n102 n101 PVC200 10 57 U1 Undergrnd n108 n98 PVC200 10 5 1(us.90); 24.31 129.31 fd10 FeedMain n98 n97 10 8 5 1(us.90); 20.98 25.98 v2 Valve n97 n96 BFV-N 8 1 DPI DPV n96 n95 DV-5 Deluge 8 1 v3 Valve n95 n94 CV-1 FIR Check 8 1 v1 Valve n94 n93 BFV-N 8 11 fd5 FeedMain n93 n92 1OGaly 8 129 1(coupling); 2.33 31.33 fd11 FeedMain n148 n130 1OGaly 8 12 1(us.Tee-Br); 40.8 42.8 m34 Cmain n146 n36 1OGaly 6 9.58 1(us.Tee-Run); m33 Cmain n 1451 n146 IOGaly 6 19.58 1(us.Tee-Run); m32 Cmain n 1441 n145 10Galy 6 9.58 1(us.Tee-Run); m31 Cmain n 1431 n144 1OGaly 6 9.58 1(us.Tee-Run); m30 Cmain n 1421 n143 1OGaly 6 9.58 1(us.Tee-Run); m29 Cmain n141 n142 IOGaly 6 9.58 1(us.Tee-Run); m28 Cmain n 1401 n141 IOGaly 6 9.58 1(us.Tee-Run); m27 Cmain n 1391 n140 1OGaly 6 9.58 1(us.Tee-Run); m26 Cmain n1381 n139 1OGaly 6 9.58 1(us.Tee-Run); m25 Cmain n1371 n138 10Galy 6 9.58 1(us.Tee-Run); m24 Cmain n1361 n137 1OGaly 6 19.58 1(us.Tee-Run); m23 Cmain n1351 n136 10Galy 6 19.58 1 1(us.Tee-Run); m22 Cmain n134 n135 IOGaly 6 9.58 1(us.Tee-Run); m21 Cmain n133 n134 1OGaly 6 9.58 1(us.Tee-Run); m20 Cmain n132 n133 lOGaly 8 9.58 1(us.Tee-Run); m19 Cmain n131 n132 10Galy 8 9.58 1(us.Tee-Run); m18 Cmain n130 n131 1OGaly 8 9.58 1(us.Tee-Run); rn36 Rnppl n36 n129 1OGaly 3 2 1(us.90); 9.41 11.41 rn35 Rnppl n146 n128 10Galy 3 2 1(us.Tee-Br); 20.16 22.16 rn34 Rnppl n145 n1 77 IOGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn33 Rnppl n 1441 n126 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn32 Rnppl n143 n125 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn31 Rnppl n142 n124 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn30 Rnppl n141 n123 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn29 Rnppl n140 n122 1OGaly 3 2 1(us.Tee-Br); 20.16 122.16 rn28 Rnppl n139 n121 1OGaly 3 2 I(us.Tee-Br); 20.16 22.16 rn27 Rnppl n138 n120 lOGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn26 Rnppl n1371 n1191 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn25 Rnppl n136 n118 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 rn24 Rnppl n135 n117 1OGaly 3 2 1(us.Tee-Br); 20.16 122.16 rn23 Rnppl n134 n116 1OGaly 3 2 1(us.Tee-Br); 20.16 122.16 rn22 Rnppl n133 n115 1OGaly 3 2 1(us.Tee-Br); 20.16 122.16 rn21 Rnppl n132 n114 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 File:VANorton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/201 a Copyright©2002-2012 Tyco Fire Protection Products Page 19 Job:Aldi South Windsor Hydraulic Calculations/Fluid Delivery Time Analysis Pipe Data Pipe Ref. Type Start End Schedule Size Length Fittings. Eq.Len. Total Len. ft ft ft rn20 Rnppl n131 n113 1OGaly 3 2 l(us.Tee-Br); 20.16 22.16 rn19 Rnppl n130 n112 1OGaly 3 2 1(us.Tee-Br); 20.16 22.16 b223 Brline h1071 h224 1OGaly 2.5 9.5 b197 Brline n129 h198 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b196 Brline n129 h194 10Galy 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b221 Brline h101 h222 1OGaly 2.5 9.5 b192 Brline n128 h193 1OGaly 2.5 114.25 1(us.Tee-Br); 16.47 130.72 b191 Brline n1281 h189 10Galy 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b187 Brline n127 h188 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b186 Brline n127 h184 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b182 Brline n126 h183 lOGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b181 Brline n126 h179 1OGaly 2.5 123.75 l(us.Tee-Br); 16.47 140.22 b177 Brline n125 h178 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b176 Brline n125 h174 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 6172_ Brline n124 h173 1OGaly 2.5- 14.25 1(as T-ee-Br); 16.4-7 30 72__ b171 Brline n124 h169 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b167 Brline n123 h168 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b166 Brline n1231 h164 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 j b162 Brline n122 h163 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 i b161 Brline n122 h159 1OGaly 2.5 123.75 11(us.Tee-Br); 16.47 40.22 b157 Brline n121 h158 1OGaly 2.5 114.25 1 l(us.Tee-Br); 16.47 30.72 b156 Brline n121 h154 10Galy 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b152 Brline n1201 h153 1OGaly 2.5 14.25 1(us.Tee-Br); 16.47 130.72 b151 Brline n120 h149 10Galy 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b147 Brline n119 h148 1OGaly 2.5 14.25 1(us.Tee-Br); 16.47 30.72 b146 Brline n119 h144 1OGaly 2.5 123.75 1 1(us.Tee-Br); 16.47 40.22 b142 Brline n118 h143 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b141 Brline n1181 h139 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 140.22 b137 Brline n117 h138 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b136 Brline n117 h134 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b132 Brline n116 h133 lOGaly 2.5 114.25 l(us.Tee-Br); 16.47 30.72 b131 Brline n116 h129 lOGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b127 Brline n115 h128 10Galy 2.5 14.25 l(us.Tee-Br); 16.47 30.72 b126 Brline n115 h124 1OGaly 2.5 23.75 1(us.Tee-Br); 16.47 40.22 b122 Brline n114 h123 1OGaly 2.5 14.25 1(us.Tee-Br); 16.47 30.72 b121 Brline n114 h119 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 b117 Brline n113 h118 1OGaly 2.5 14.25 1(us.Tee-Br); 16.47 30.72 b116 Brline n113 h114 1OGaly 2.5 23.75 l(us.Tee-Br); 16.47 40.22 2 Brline n112 h113 1OGaly 2.5 14.25 l(us.Tee-Br); 16.47 30.72 bill I Brline n112 h109 10Galy 2.5 23.75 1(us.Tee-Br); 16.47 40.22 File:V:Worton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright 0 2002-2012 Tyco Fire Protection Products Page 20 Job:Aldi South Windsor Device Graphs Pressure vs. Flow Function Headset: Headset_1; Supply Ref.: src1; Supply Name:discharge outlet 200 ,._. 190_. __. ..-. _.... .... - -__. ........ - 180" _ . ...-... ._ ...... 170 . „. ..�,.,... 160 ..,..__ ...,_..�. .,..r_.... _ ._._.... -.._._ . ....___ ., ..__......, 140_ ., .._.: ,. .., ...,:.. _. •U 130 .._..._.,,. _i.,..,,._.. .,,....._.__ ......_.w._._ N _ 100 _... L 80 ..... _.,,� _ .... . . . ,........_... _.... 70 ,-..... ........._ ___., __...,_._. _ ..____.. ....._.._.... ......_.,_ .._._...m.. _._�__,_. �..,._.... __..,_�_� __..� - 60 40 - 30 . .. ..._....: ._.,,_.,.:.., .... .....�..:...... ..._.__.:y. 20, _:.,, _....._... _.,: _.,. ........,.,, 10 . ... ...... .. ............ ... .._:_..... ..., :,......,., ::.:... ..., 0 0 0 0 0 Flow,gpm Pressure Loss Function Headset: Headset_1; DPV Ref.: DPI (DV-5 Deluge, Size = 8); Inlet Node: n95; Outlet Node: n96 8.57'- 6.57- ............._ CL - - i 5.57- ._._.._...,. .... y y 4) 4.57.. ..........._ ._.:.__.... ......_, ..._....__ ....._..., ..... ........_. ....._..,._....._...... ..... -._.M ._. a 3.57_ _....., .,. .., . . _ 2.57_. . . ... .. ...... _ 1.57... ...... ......... ..._.__ 0.57_. _ _ —' '� �• N A M c<t Y Flow,gpm File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip caics\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 21 Job:Aldi South Windsor Device Graphs Pressure Loss Function Headset: Headset_!; Valve Ref.. vi (RFV-N, Size = 81; inlet Node: nq3; Outlet Norte: n94 rL v 1.299- N N Q1 0.799 0.299 L a K � K Flow,gpm Pressure Loss Function Headset: Headset_1; Valve Ref.: v2 (BFV-N, Size = 8); Inlet Node: n96; Outlet Node: n97 1.799 m. _ ._..,.__.... _. , .. .. ..>.:._._ ._...._ _._ ....._. .., ._ _. .. CL 0 N $D a` 0.799 Flow,gpm File:V:\Norton Drawings\09 Brian M\Brian's Drawings\Aldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright 0 2002-2012 Tyco Fire Protection Products Page 22 Job:Aldi South Windsor Device Graphs Pressure Loss Function Headset: Headset_1; Valve Ref.: v3 (CV-1 FR Check, Size = 8); Inlet Node: n94; Outlet Node: n95 4.5_ .. _.,�....... .. _.. ,.._.._., m 3.5 CL ._...._...... .�..,...._.... .,....._,.._ ... . ........�.. ,.. .._. .. L N N ti 2.s 1.s 25 �.._.._.. .,.._...�_ o 0 0 h h Flow,gpm File:V:\Norton Drawings\09 Brian M\Brian's DrawingsWldi South Windsor\CALCS\trip calcs\sys 1.tyc3 Date 3/2/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 23 it 1