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175 Oakland Road - Building Plans & Draw
,.J k Fire Protection by.Computer Design ENCORE FIRE PROTECTION zlc.r�o.cta `� 11.0 MURPHY ROAD 5I„Iftt+t RA HARTFORD CT 061.14 - 8602467711 .lob Name 2-SPI-17005 BUILDING 1 CALC Drawing 1 Location 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Remote Area 1 Contract 2-SPI-17005 Data File 2-SPI--17005 BUILDING 1 CALG Area-1,WXF i ,,a Computer Programs by Hydratec Inc. Route:I I1 Windham N.H.USA 03087 T- ENCORE FIRE PROTECTION Page- 1 2-SPI-17005 BUILDING 1 CALC Date HYDRAULIC DESIGN INFORMATION SHEET y Name - 175 OAKLAND ROAD Date - 1-31-2017 Location - 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Building - 1 System No. - 1 Contractor - ENCORE FIRE PROTECTION Contract No. 2-SPI-17005 Calculated By - JA Drawing No. - FP-2 Construction: (X) Combustible ( ) Non-Combustible Ceiling Sleight 9'0" OCCUPANCY - RESIDENTIAL S: Type of Calculation: (. )NFPA 13 Residential (X)NFPA 13R ( )NFPA 13D Y Number of Sprinklers Flowing.: ( }1 {. ):2 {X)4 S, ( )Other T { )Specific Ruling Made by Date., N5 Listed Flow at .Start Point - 21 Gpm System Type: Listed Pres. at Start Point - 25 Psi ('X) T.-let ( ) Dry D MAXIMUM LISTED SPACING 1'6' x 18` { ) Deluge ( ? Pr:eActi.on E Domestic- Flow Added. - GpmSprinkler or. Ilozzle: S Additional Flow Added Gpm Make TYCO Model LFII I Elevation at Highest outlet - 1.8..83Feet Size 1/2" K-Factor 4.,'2 G Note Temperature Ra,tincg 155. N Calculation Gpm Required M 38-7 Psi Required> 90.837 At Test summary C'-Factor Used: Overhead 15.0 Underground 150 W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - 1997 Rated Cap. Cap. T Time :of Te.s:t - Ps:i Elev. E Static (Psi) - 118 Elev. R Residual (Psi). - 98 Other Well. FlowjGpm) - 19$0' Proof Flo: Gpm S Elevation - 0 `Y P Location: OAKLAND ROAD P L Source of Information: MDC HYDRANT FLOWW, RECORDS Y } Computer Programs by Hydratec Inc. Route 111 Windham N.H.USA 03087 L Water Supply Curare C ENCORE FIRE PROTECTION Page 1 2-SPI-17005 BUILDING 1 CALC Date City Water�5uppiy: Demand: C1 -Static Pressure 118 Q1 -Elevation 155 C2-Residual Pressure: . . 98 D2 System Flow 88.155 C2-Residual low 1980 D2-System Pressure : 90.837 Hose(Demand) D3-System Demand :89.387 Safety,Margin 27.098 1,50 140 130 p 120 C1 t R 110 E 100 D2 S 90 S 80 u 70 R 60 E 50 40 t 30 20 10 ' C!1 200 400 600 800 1000 1200 1400, 1600 1800 FLOW(:NAJ.85} Computer:Programs by Hydratec-Inc. Ro4te.111 Windham N.H.USA. 030$7 Fittings Used Summary Page 2 ENCORE FIRE PROTECTION Date 2-SPI-17005 BUILDING 1 CALC Fitting Legend 3 3% 4 5 6' 8 _10__-- 12 -- 14 16 18 20 24 Abbrev. Name 2 2%2 -- NFPA 13 90'StandGrd E"bow 1 2 2 3 4 5 6 7' 8: 10 12 14 1$ 22 27 35 40 45 50 61 Fitting generates a Fixed Loss Based on Flow Fsp Flow Switch Potter VSR G NFPA 13 Gate Valve 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 11 13 4 T NFPA 13 90`Flow thru Tee 4 6 6 8 'I O 12 1'5 /7 20 25 30 35 50 60 71 81 91 91 101 121 Zaa Ames 2000E Fitting generates a Fixed Loss Based on Flow Units 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 length$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. Route 111 Windham N.H. USA 03087 Pressure'/Flow Summary STANDARD ENCORE FIRE PROTECTION Page 3 2-SPI-17005 BUILDING 1 CALG Date Node Elevation K-Fact Pt Pn Flow Density Area Press Actual No. - Actual _._ ECG--- . 1 18.83 4.2 25:44 na 21.18 0.06 40.43 25.0 2 9.67 31,99 na 3 9.67 32.51_ na 4 9.67 43.46 na 5 9.67 46.33 na TOR 9.67 14.17 na BOR 1.0 83A5.. na UG1 1.0 9006 na UG2 -5.0 92:7 na UG5 -5.0 92.98 na TEST O.O 90 84 na 7 18.83 4.2 25.0 na 21.0 us 241 26.0 _ 8 9.67 31;49. na 9 98.83 4:2 26.3:3 na 21M 0.05 229 25:O 1.0 18.83 4.2. 37.3 na 25M. 0.05 47:5 25.0 11 9:67 44.22 na J I The maximum velocity is:21:4:t3 and it occurs in the pipe between nodes 3 and .J I i j i i I I i J J i _J I I ..J _ Computer Programs by Hydratec Inc. Route 111 Windham N.H.USA 03087 Final Calculations - Hazen-Williams -2007 ENCORE FIRE PROTECTION Page 4 Date 2-SPI-17005 13OILDING 1 CALC Node1 Elev1 K Qa Norn Fitting Pipe CFact Pt £* %* to or _ Ftnys Pe * * Notes Node2 Elev2 Fact Qt Act Eqv, Ln. Total Pf/Ft Pf 1 18.83 4.20 21,18 1 E 3.825 11 A 20 1.50 25.442 _ to 2T 19.125 22.951 3.967 2 9.67 21.18 1.101 0.6 34.071 0.0757 2.579 Vel= 7.14 -2 9.67 21.00 1 0.0 1.940 150. 31.98& _ to 0.0 0.0 0.0 3 9.67 42.18 1.101 _ 0.0 _ 1.940 0,2706 0.525 Vel= 14.21 3 9.67 21,56 1 T 9.663 9.290 150 32.613 to 0.0 9.662 0.0 4 _9.67 63.74 1.101 0.0 18.852 0.5807 10:948 Vel= 21.48 4 T 9.67 0,0 1.25 0.0 15.590 150 43.461 to 0.0 0.0 0.0 5. 9.67 63.74 1.394 0.0 15:590 0.1841 2,870' Vel= 13.40 5 9,67, 25.65 1.25 2E 9.523: 71.370 150 46.331 to 0.0 9.523 0.0 TOR 9..67 89.39 1.39.4 0.0 80.893 0.3441 27.834' Vel`= 18.79 TOR 9.67 0.,0 1.5 Fsp 00 8.667 120 74.165 to 0.0 0,0 6.755> "*Fixed Loss=3 _BOR 1` 89.39 1.6 I 0:0 8.667 0,2578 2.234 Vel= 14.09 _ BOR �1 0.0 1.5 Zaa 0A 0.010 120 83.154 to: 0.0 0.0 6.900 *}Fixed Loss=69 UG1 1 $9 39 1.61 0,0 0,010 0.3000 0.003 Vel= 14.0.9 UG1 1 0.0 4 E 14.534 6.000 140 90,057 to 0A 14.5M, 2.599 UG2 -5 89.39 4.1 0.0 20.584 0,0020 0.042 Vel= 2117 UG2 -5 0.0 4. E 14♦534 90.000 140: 02.608 to G 2.007 46,508 0.0 UG5 5 89,39 4.1 T 29.067 136,508` 0.0020 0_279; Vel= 2.17 UG5 . 0.0 8 2G 12,662 '240.000 - 140 92.977 to 2T 110.709 151.829 2,166 TEST 0 89.39 8,27 E 28,468 391.82:9' 0.0001 0.026` Vel= 0:53 _. T 00 TEST 8 .0 90.837 K Factor= 9..38 7 18.830 4.20 21.00 1 T 9.563 20.458 150' 25,000 to E 3,825 13.387 3.967 8 9.670 21.0 1.101 0.0 33_845 --0.0745 2.52:1 Vel= 7.08 ----- - --8----9.670 ------- 0.0_._ 1 0.0 6.720 150 31.488 to 0.0 0.0 0.0 2 9.67 21.0 1.101„ 0_0 -6.720 _- 0.0744 0.500 Vel= 7,08 U:0 ...� 21:00 31 988 K Factor 3� 71 _ 9_._.-__t8.83 - 4,20 ' 21.55 'i 2E 7.65 1 1 120 '150 26.332 to T 9.563 17,212 3.967 _. 3 9.67 21.55 1.101 0 0 28.332 0.0781 2,214 Vel= 7.26 --3201 55 32_513 _K Factor=_3.78 10 18.83 4.20 25.65 1 2E 7.65 10.170 160 37.298 to T 9.563 17.212 3.967 11 9.67 25.65 1,101 0.0 27,382 0.1078 2,952 Vel 8.64 Computer Programs by Hydratec Inc. Route 111 Windham NA USA 03087 Final Calculations - Hazen-Williams ENCORE FIRE PROTECTION Page 5 2-SPI-17005 BUILDING 1 CALC Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe Notes ** � --� Node2 Elev2 Fact Qt Act Egv. Ln. Total Pf/Ft Pf 11 9.67 0.0 1 T 9.563 10.040 150 44.217 -- to 0.0 9.562 0.0 5 9.67 25.65 1.101 0.0 19.602 0.1078 2.114 Vet= 8.64 - --.w 0.0' 5 25.65 M 464 331 K Factor= 3.77 J J 3 f J i i J i i i J J j I J i __j Cornprrter Programs.by Hydratec Inc. Route 111 Windham N.H.USA 03087 General Calculation Program Job - 2-SPI-17005 BUILDING 1 CALC Date - 02/03/17 File - C:\HES\HydraCALC\Ver50\Data\Jobs.\2-SPI-17005 BUILDING 1 CALL Area l.WXFTime 10:08:49 AREA CALCULATED HEAD FLOV-1 SUMMARY Actual Ricq.: Delta Actual Req. Delta Flow Flow. Press. Press. ID K Factor Flow Press 1 4.200 21.18 21 .00 0.18 .2.5.442 Pt 25.000 0.442 7 4.200 21.00 21.00 0.00 25..000 Pt 25.Ho 0.000 9- 4.2.0G 21.55 21 .0.0 0.55 26.332 Pt 25.000 1.332 10 4.200 .25. 6:5 21.00 4.65 37.298 Ft: - 25.000 12.298 Total K Factor's. 4 Total Fixed Flows:. 0 Sum Actual Flow, 89.3-9 Sum Required. Flow. 84 .0 Sum Delta Flour . . . 5.3:9` Max Delta Flow . . . . 4.65 Max .Delta Pressure , 12.298 i AREA CALCULATED - COM-PLETE SUMMARY Start Finish Diam. Start normal Pf Elev/Fix;ed Flow Vel P Pres. Pres. Point Point Pres. 2.579 3.>967 1 �_ 2 1.101 25.442 21.18 7.14 0.525 0.000 2 <- 3 1 .101 31.988 42 .18 14 .22 3 <._ 4 1.1.01 32.513 10 .948 0.000 63.74 2:i_.48 2.869 0.000 11 <- 5 1. . 394 43-.461 63 .74 1 .3.e10 5 < If OR 1 . 394 46. 331 2"X .834 0.000 89.39 18.79 2 .234 6.755 TOR <- BOR 1 . 610 74 .165. 89.39 14.09 0.003 6.900 BOR <- UG1 1. 610 83.154 i J 89. 39 14.09 UG1 <- UG2 4 .100 90,0.57 0.042 2. 599 89.39 2. 17 UG2 <- UG5 4.100 92. 698 0.279 0.0.00 89.39 2.17 UG5- <- TEST 8.270 92.977 0.026 -2: 165 89.39 0.53 7 <- 8 1.101 25.000 2.520 3.967 21. 00 7.08 8 < 2 11101 31.488 0.500 0.000 21.00 7.08 9 <- 3 1.101 26.332 2-214 3.967 21..55 _ 7..26 10 <- 11 1.101 37.298 2.952 3.967 25,"65 8. 64 5 1.10`1 4 4,,217 2..113 0.000 25.65 8. 64 Pipe with h,ighest velocity:, 3. - 4 (21.479) _i Water Supply Summary @ Point TEST Total Flory From tsTate:r S,upp;ly Curve; 89.387 Pressure From Water Supply Curve 117.935 System Pressure Demand At Supply Curve . . 90.837 t Safey Margin at `Su 1 Curve.. ' ..� '-Supply 27098 J I J .-J i i J , 1 2 J n _ J �., -y J J i I i i i i J I i j Fire Protection by Computer Design 4 ENCORE FIRE PROTECTIONLt0.td0.pyt37�', 110 M.URPHY ROAD STA OF HARTFORD CT 06114 so 8602467711 J ..s.J 1 j Job Name 2-SPI-17005 BUILDING 2 CALC 1 J Drawing 2 Location 175 OAKLAND ROAD SOUTH WINDS'OR CT 06074 Remote Area : 1 j Contract 2-SPI-17005 _ 1 Data File : 2-SPI-17005 BUILDING 2 CALC Area 1.WXF i i J j J Computer Programs by Hydratec Inc. Route 111 Windham N.H, USA 03087 ENCORE FIRE PROTECTION Page 1 2-SPI-17005 BUILDING 2 CALC 1 Date HYDRAULIC DESIGN INFORMATION SHEET Name - 175 OAKLAND ROAD Date: 1-31-2017 Location - 175 ;OAKLAND ROAD SOUTH WINDSOR CT 06074 Building 2 System No. - 1 Contracto - ENCORE FIRE PROTECTION Contract No.. 2-SPI-17005 r Calculated By - JA Drawing No. - FP-3 Construction: W Combustible ( ) Non-Combustible Ceilinq Height 9'0" OCCUPANCY - RESIDENTIAL S Type of Calculation: ( )NFPA 13 Residential (X)NFPA 1.3R ( )NFPA 13D Y Number of ,Sprinklers Flowing-, ( ) 1 ( )2 (X)4 S ( )Other T ( )Specific Ruling Made by Date: E M Listed Flow at Start Point - 21 Gpm System Type- Listed Pres. at Start. Point - 25 Psi (X) Ttlet ( ) Dry D MAXIMUM LISTED 'SPACING 16' x 18' ( .) 'Deluge ( ) PreAct on El Domestic Flow Added - Gpm Sprinkler or Nozzle S Additional F1o5�' Addad - Gpm Make T`!CO Model LFII. I Elevation at Highest Outlet - 18..83Feet Size 1/21 K-Factor 4.2 G Note: Temperature Rating 155 `j Calculation Gpm Required 90."545 Psi Required 106-.3.53 At Test Summary G-Factor Used: Overhead 150 tjitderground 150 W Water Flow Test: Pump Data•: Tank or Reservoir: A Date. of Test _ 1997 hated Cap.. Cap. T Time of Test - @ Psi Elev. E Static (Psi) - 118 Elev. - R Residual (Psi) 98 Other Well Flow (Gpm) - 198:0 Proof Flow Gpm j S Elevation - 0 P Location OAKLAND ROAD P L Source of Information: MDC HYDRANT FLOW RECORDS Y Computer Programs by Hydratec Inc. Route ill Windha►n N.H.USA 03087' Water Supply Curve C ENCORE FIRE PROTECTION 2-SPI-17005 BUILDING 2 C,4LC 1 Page 2 Date' City Water Supply: Demand: C1 -Static Pressure 118 D1 -Elevation 722 C2-Residual Pressure: 9$ D2-System Flow 97..722 C2-Residua! Flaw 1980 545 D2-System Pressure ,: 106,353 Hose(Demand) D3-System remand :90545 Safety Margin 11,580 150 140 130 P 120 C1 I R 110 I F 100 S 90 Ell' C 2 S 80 U 70 R 60 E 50 1 40 30 20 10 ©1 200 400 600 500 1000 1200 1400 1600 1800 FLOW(N^ 1,85 Computer'Programs by Hydratec Inc. Route.111 Windham N.H. USA, 03057' Fittings Used Summary Page 3. ENCORE FIRE PROTECTION Date 2-SPI-17005 BUILDING 2 CALG 1 Fitting Legend .6 8 10 12 14 16 18 20_ 24 Abbrev. Name f -----g� 7 $ 1Q 12 14 t'8 22 27 35 40 45 50 61 "/;._...?--2"/x; 3 3"f' 4 5 E NFPA 13 90'Standard Elbcw 2 2 3 4 5 6 Fsp Flow Switch Potter VSR Fitting generates Fixed Loss o 1FIow 1 1 1 2.: 2 3 4 5' 6 7 8 10 11 13 G NFPA 13 Gate Valve 0 0 0 0 0 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 Zaa Ames 200013' ;tting generates a Fixed Loss Based on.Flow, Units Summary Diameter Units Inches Length Units Feat Flow Units US Gallons per Minute Pressure Units PIounds 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., Computes Programs byHydratec Inc. Route 111. Windham N.H.USA 03087 Pressure 1 Flaw Summary-STANDARD ENCORE FIRE PROTECTION Page 4 2-SPI-17005 BUILDING 2 CALC 1 Date Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Reg. J , 1 17.83 42 25.0 na .21.0 0.05 224.01 25.0 2 18.83 24.93 na 3 9.67 30.25 na J 4 9.67 36.5 na 5 9.67 48.62 na TOR 9.67 87.87 na. BOR 1.0 98.5 na UG1 1.0 '105.6 na UG2 -5.0 108.25 na UG3 5,0 108.48 na TEST 0.0 106.35 na 7 17.83 41 25.08 na 21.03 0,05 41.1 25.0 8' 18.83 25,0 na 9 17.83 4.2 29:53 na 22.82 0:05 190.31 25.0 10 1863 29.52 na 11 17 83 4.2 37.41 na a69° 0.05 46126 25;0: 12 18.83 37.5 na 1 13 9.67 44.63 na 14 9:67 46.71 na 1 I i The maximum velocity is 21.86 and it occurs in the pipe.between nodes 4 and J i J i i i i J Computer Programs by Nydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hawn-Williams - 2007 ENCORE FIRE PROTECTION Page 5 2-SPI-17005 BUILDING 2 CALC 1 Date Node1 Elev1 K Qa Nom Fitting _ Pipe CFact Pt to or Ftng s Pe Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf1Ft Pf 1 17.83 4.20 21,00 1 E 3.826 1.000 150 25.000 to 0.0 3.825 -0.433 2 16.83 21.0 1.101 0.0 4.826 0,0744 0.359 Vela 7.08 2 18.83 0.0--�1_.� 2E 7.65 10.610 150 24.926 to 0.0 7.650 3.967 3 9.67 _ 21.0 1.101 0.0 18.260 0,0745 1.360 Vel= 7.08 3 9.67 21,03 1 2T 19.125 4.120 150 30.253 to 0.0' 19.126 0.0 4 9.67 42.03 1.101 0.0 23.246 0.2688 6.249 Vel`= 14.16 4 9.67 22.83 1 T 9.563 10.640 150 36.502 to 0:0 9.562, 0.0 5 9.67 64.86 1.101 0:0 20.202 0.5998 12.117 Ve[= 21.86 5 9.67 25.68 1.25 T 9.523 78.070 150 48.619 to 5E 23:808 $3,331 0.0 TOR 9..67 90.54 1.394 0.0 111.401 0.3524 39.255 Vel= 19.03 TOR 9.67 0:0 1.5 Fsp 0.0 14.670 1.20 87.874 to. 0.0 O:0 6.755 " *,Fixed Loss-3 BOR 1 190.54 1.61 0.0 14.670 0.2640 3.873 Vel= 14.27 BOR 1 -0:0 1:5. Zaa 0.0 0.010 120 98.502 to 0.0 0.0 7.100 Fixed Loss 7.1 UG1 1 90.54 1.61 0.0 0.010 0-.3000 0.003 Vel 14.27 UG1 1 0.0 4 E 14534 6.000 140 105.605 w to 0.0 14:534 2.599. UG2' -5 90.64 4.1 0.0 20.534 0;0020 0.042 Val= 2.20 UG2 -5 0.0 4 G 2.9.07 MOM 140 168,246'to T 29.067 31.074 0.0 UG3 -5 90.54 4.1 0.0 111.074 0.0021 0.234 Vel= 2.20. UG3 -5 0.0 8 2E .56.936 436.000 140 108,480 _ to 2G 12.652 124,942 4.166. TEST 0 90.54 8.27 T 55.354 $59.942 0.0001 0.039 Vel= 0.54 0.0 TEST 90,54 106.353 K Factor= 8.78 7 17.83 4.20 21.03 1, E 3.825 1.000 150 25.075 to 0..0 3,825 4433 8 18.83 21.03 1,101 0.0 4.826 0.0.746 0.260, Vel= 7.09 -_- _--_ - -- - 8 18.83 0.0 1 2E 7.65 9.640 150 25.002 to 0.0 7.650 3,967 3 9,67 21.03 1.101 0.0 17.190 0.0747 1284 Vel 7.09 0.0 30 253 K Factor= 3 82 3 21,03 _ _ .-._...._ ---- ...... ..... 9 17.83 4.20 22.82 1 E 3.826 1.000 150 29.534 to 0.0 3.825 -0.433 10 18.83 22_82 1.101 0.0_ 4.825-- 0.0868� 0.419 Vel= 7.69 10 18.83 0.0 1 3E 11,475 23.230; 150 HMO to 0.0 11.475 3,967 4 9.67 22.82 1,101 0.0 34.705 0.0869 3,015 Vel= 7.69 0.0 4 22•82 36.502 K Factor= 3.78 Computer Programs by Hydrates Inc. Route 111 Windham N.H. USA 03087` Final Calculations Hazed-Williams ENCORE FIRE PROTECTION Page 6 2-SPI-17005 BUILDING 2 CALC 1 Date Node1 Elev1 K Qa Nom Fitting _ Pipe CFact Pt to or Ftng's Pe taa*xt Notes tyre Node2 Elev2 Fact Qt Act Eqv. Lm Total Pun Pf 11 17.83 4.20 25.69 1 E 3.825 1.000 150 37.409 to 0.0 3.825 -6.433 12 18.83 25.69 1.101 0..0 4.825 0.1080 0.521 Vel= 8.66 -� 12 18.83 0.0 1 2E 7..65 12.060 150 37.497 to T 9.563 17.212 3.967 13 J,67 25.fi9 1.101 0.0 29.272 0.1081 3.165 Vel= 8.66 13: 9.67 0.0 1 T 9.563 9.680 150 44.629: to 0.0 9.562 0.0 14 9.67 25.69 1.101 0.0 19.242 0.1081 2.081 Vel, 8.66 14 9.67 0.0 1 0.0 17.660 150 46.710 t° 0.0 i 5 9.67 25.69 1.101 0.0 17.660 0.1081 1.909' Vet 8.66 !_ _ . o;q l 5 25;69 48.619: K Factor 3.68 Jt ,-i 3 ? J i i i I i i J Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 General Calculation Program Job - 2-SPI-17005. BUILDING 2 CALC 1 Date - 02/03/37 Filer C: \HES\HydraCALC\Ver5.0\Data\Jobs\2-S>PI-17005. BUILDING 2 CALL Area 1 .WXFTime - 12:57,34 AREA CALCULATED - HEAD FLOW SUMMARY Actual Req. Delta Actual Req. Delta ID K-:Factor Flow Flow Flow. Press, Press. Press 1 4.200 21.00 21..00 0.00 25.000 Pt 25.000 0.000 7 4..200 21.03 21.00 0.03 25.0-75 Pt 25.000 0.075 9 4-200: 22.82 21.00 1.82 29.53:4 Pt. 2 5..0:0'0 4 .534 11 4.200` 25. 69 21 .00 4.69 37.4'09' Pt 25.000 12.409 Total K Factors. 4 Total Fixed Flows. 0 Sum Actual Flog. 90.54 Sum Required. Flow. 84.00. Sum Delta Flow" 6.54 Max Delta Flow 4.69 Max Delta Pressure 12.409 AREA CALCULATED - COMPLETE SUMMARY Start Finish Diam. Start Normal Pf Elev/Fix.ed Flow Vel Point Point Pres.. Pres. _ Pres. 1 < 2 1 .101 25.000 0.359 -0..433 21 .0`0 7. 08 2 <- 3: 1.101 24 .926 1 .360 3.967 2.1 .0.0 7.08 3 <- 4 1. 101, 30'.253 6. 249 0.000 42 .03 14 . 16 4 <- 5 1 . 101 36.502 12 .116 0.000 �- 64 . 8C 21 .8 TOR 1 .394 48. 61.9 39.25b 0.000 90. 54 19.03 - TOR <-- BOO 1 .610 87 .874 3. 873 6.755. 90 .54 14 .27 BOR <- UG1 1.610 98.502 0.003 7. 100 90.54 14 .27_ UG1 < UG2 4 . 100 105. 605 90.54 2.20 0.043 2.599 UG2 <- UG3 4.100 108.246 0.234 0.000 90.54 2.20 UG3 <- TEST 8.270 108.4€30' 0.038 -2, 165 90.54 0.54 7 <- 8 1. 101 25.075 0.3'60 -0. 33 21.03 7.09 1.101 25.002 1 .28:4 3.967 21 ,03 7.09 9` <- 10 1.101 29.534 0.419. -0:433 22.82. 7. 69 10 <- 4 1. 101 29.520 3.015 3.9:67 22.8.2 7. 69 11 <= 12 1. 1,01 25.6 37:4Q9 0,.522. -0.433 9. 8. 66 12 <- 13 1.101 37.497 3.165: 3.967 25.69 8.66 13 <- 14 1.-101 44. 62-9 21.080 0.00.0 25.69 8.66 14 <- 5' 1,101 46.710 j 25.69 8,&6r 1.909 0.000 Pipe with highest velocity; :4 - 5 (21.856) I Vater supply Summary @ Point TEST Total Flog From Water Supply Curve 90.54.5 Pressure From Water Supply Curve 117.934 System. Pressure Demand At supply curve 106.353 Safety Margin at Supply Curve, 11.560 i it i 2 J I i i I i r i J t .. Fire Protection by Computer Design ,r ENCORE FIRE PROTECTION �� GtQ t�0.OG019, q, 574t�,t�'Chx,�'.it� 110 MURPHY ROAD C)iat'+DN h3h 'p HARTFORD-CT 06114 -� 86024.67711 �' i i Job Name 2-SPI-1.7005 BUILDING 2 CALC 2 Drawing 2 Location 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Remote Area 2 Contract 2-SPI-'17005 Data File 2-SPI-17005 BUILDING 2 CALC Area 2.WXF I J Computer Programs by Hydratec Inc. Route 111 Windham N.H. -USA 03087 ENCORE FIRE PROTECTION Page 1 2-SPI-17005 BUILDING 2 CALC 2 Date HYDRAULIC DESIGN INFORMATION SHEET _. Name - 175 OAKLAND ROAD Date - 1-31-2017 Location - 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Building - 1 System No. - 2 Contractor - ENCORE FIRE PROTECTION Contract No. - 2-SPI-17005 Calculated By - JA Drawing No. FP-3 Construction: (X). Combustible ( ) Non-Combustible Ceiling Height 9'0" OCCUPANCY - RESIDENTIAL S Type of Calculation: ( )NFPA 13 Residential (X)NFPA 13R { )NFPA 13D ;- Y Number of Sprinklers Flowing: t )l (X,)2 ( )4 ( ) S ( )Other T ( )Specific Ruling Made by Date G M Listed Flo:r at 'Start Point - 21 Gpm System Type _ Listed Pres.. at Start Point - 25 Psi (X) Wet t ) Dry D MAXIMUM LISTED SPACING. 16' x 18' { ) Deluge { ) PreAction E Domestic Flow Added - Gpm Sprinkler or Nozzle — S Additional Flow Addeel. - Gpm Make TYGO Model LFII I Elevation at Highest Outlet - 18.83Feet Size 1/2'" K-Factor 4.2 G Note: Tempe°rat:ure Rating 155 N Calculation. Gpm Required 42.201 Psi Required 69.347 At Test Summary C.-Factor Used: Overhead 150. Underground 150' — Y] Water Flow Test: Pump Data: Tank o:r .Reservoir: A Date of Test - 1997 Rated Capi Cap. T Time of Test @ Psi Elev. E Static ,(Psi) 118 Elev. R: Residual (Psi) - 98 Other Well Flow :{Gpm) - 198T? Proof Flow Gpm S Elevation - 0 P Location: OAKLAND ROAD P L Source of Information: MDC HYDRANT FLOW RECORDS- T Y Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Water Supply Curve C ENCORE FIRE PROTECTION Page 2 2-SPI-17005'BUILDING 2 CALC 2 Date City Water Supply: Demand: C1 -Static Pressure 118 D1 Elevation 7.722 C2-Residual Pressure: 98 D2-System Flow :42:201 C2-Residua! Flow 1980 ©2-System Pressure 69.347 Hose(Demand) D3-System Demand ;42.201 Safety Margin : 48.636 150 140 130 p 1.20 C1 R 110 E 100 S :90 S 80 D2 U 70 R 60 E 50 40 30 20 10 D1 200 400 600 800 1000 1200 1400 1600 1800 FLOW(NX1.85) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 0$087 Fittings Used Summary lary ENCORE FIRE PROTECTION Page 3 2-SPI-17005 BUILDING 2 CALC 2 Date Fitting Legend Abbrev. Name %_ '/ 1 1'/< 1'✓Z 2 2%z 3 31%, 4_-_'5 6 8 10 12 14 16 18 20 24 E NFPA 13 90'Standard Et"ovi 1 2 2 3 4 5 .6' 7 8 10: . 12 14 18 22 27 Z5 40 45 60 61 Fsp Flow Switch Potter VSR Fixing generates a Fixed Loss Based on Flow 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 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 14 121, 15 17' 20 25; 30 35 5.0 60 71 81 91 101 121 Zaa Ames 2000E Fitting generates a.Fixed Loss Based on Flow Units Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute. Pressure Units Pounds per Square Inch Note: Fitting Legend provides e,quiva! rit 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 regdire no adjustment All values for fittings not marked with a*will be adjusted in the calculation for CFactors of other than 1.20 acid diameters other than Sched 40 per NFPA. Computer Programs by Hydretec Inc. Route 1:11 Windham N.H.USA 03087 . f — Pressure/ Flow Summary- STANDARD ENCORE FIRE PROTECTION gaga 4 2-SPI-17005 BUILDING 2 CALC 2 ©ate . Node Elevation K Fact Pt Pn Flow Density Area Press, No. Actual _Actual Req 15 17.83 4.2 25.0 na 21.0 0,05 21 25:0 16 18,83 24.93 na 17 9.67 31.57 Ra 18 9.67 31:74 na 19 .-5.0 54.22 na 20 5.0 59.23 na TOR 9.67 56:39 na SOR 10 64.06 na UG1 1.0 68.82 na UG2 :5.0 71:45 na UG3 -5.0 71.5 na TEST 0.0 69,35 na 21 17.83 4.2 25.48 na :21.2 0.05 124 25.0 22 18.83 25:12 na 23 9.67 30.89 na i i i -� The maximum velocity is 10.77 and it occurs in the pipe e between nodes 19 and 20 i - ;p i i -J E i i i �l J i Computer Programs by Hydratec Inc. Route ill Windham N.H: USA 03087 Final Calculations - Hazen-Williams - 2007 ENCORE FIRE PROTECTION Page 5 2-SPI-17005 BUILDING 2 CALC 2 Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt _ to or Ftng's Pei* * Notes «* ** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 15 17.83 4.20 21..00 1 E 3.825 1.000 150 25.000 to 0.0 3.825 -0.433 16 1.8.83 21.0 1.101 0.0 4.825 0.0744 0.359 Vet= 7.08 16 18.83 0.0 1 E' 3.825 12.990 150 - 24.926 to 2T 19.125 22,951 3.967 17 9.67 21.0 1.101 0.0 35.941 0.0745 2.677 Vel= 7.08 �17 - 9.67 0.0 1.25 0.0 7.1.50 150 31:570 to 0:0 0.0 0.0 18 9.67 21,0 1.394 0.0 7.150 0.0236 0.169 Vel= 4.41 18 9.67 21.20 1.25 6E 28.57 130.810 150 31.739 to 3T 28.57 57.138 6.354 19 75 42.2; 1,3.04 0.0 187,948 0.0858 16,131 Vet= 8.87 19 -5 0.0 1.26 2E 6.935 30.375 M 54.224 to 0.0 5.935 OA 20 =5 42.2 1.266 0.0 36.316 01377 5.001 Vel 10.77 _ -- 20 -5 0.0 1.25 3E 11,148 13.375 120. 59.225' to T 7.432 18.580 -0,354 TOR 957 422 1.442 0.0 31.955 0.1100 3.515 Vel'= 8.29. TOR 9.67 0.0 1.5 Fsp 0.0 14.670 In 56.386 to 0:0 0.0 6,755 **Fixed Loss=3 BOR 1 42.2 1.61 0.0 14.670 0.0643 0.944 Vel= 6.65 BOR 1 0`10 1.5- Zaa 0.0 0.010 120 64.085 to 0.0 0.0 4.738 ""'Fixed Loss.=4.738 UG1 1 42,2 1.61 00 0.010 0 00 Vel= 6,.65. . UG1 1 0,0 4 3E 43,601 6.000 140 68.823 to 0.0 43.601 2.599 UG2 -5 42.2 4.1 0.0 49.601 0.000.5 0.024 Vet= 1.03: UG2 =5 0.0 4 G 2.907 80.000 140 71.446 to T 29.06.7 31.974 0.0 UG3 -5 42.2 4.1 0.0 111.974 0.0006 0.060 Vel= 1.03 UG3 -5 0.0 8 2E 56.936 435,000 140 71.504 to 2G 12.652 124.942 -2.166 TEST 0 42.2 8:27 T 55.354 559.942 0 0.009 Vel 0.25 0.0 TEST 42.20 - 69.347 K_ Factor= 5.07____. .------- _ 21 17,83 4,20 21.20 1 0.0 1,000 150 25.480 to 0.0 0,0 0 433 22 18.83 21.2 1.101 0_0 - 1.000 0.0760 0,076 Vel " 7.14 _--- ____..---._. .__ . .._. - _ .._._ 22 18.83 0.0 1 E 3.825 10.430 150 25.123 `r to T 9.563 13.387 3.967 23 9.67 21.2 1.10`1,_ 0.0 23.817 0.0758 1.805 Vol .14 23 9.67 0.0 1 T. 9.563 1,570 150 30.895 to 0.0 9.562 0.0 18 9.67 21.2 _ 1.101 0.0 11.1.32 0.0758 0,844 Vet= 7,14 0.0 18 21.20 31.739' K Factor 3.76 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 General Calculation Program Job - 2-SPI-17005 BUILDING 2 CALC 2 Date 02/03/17 File - C.: \BES\HydraCALC\Ver50\Data\Jobs\2-SPI-17005 BUILDING 2 CALL Area 2.WXFTime - 13:08:24 AREA CALCULATED HEAD FLOW SUMMARY Actual Req. Delta Actual Req, Delta ID K Factor Flow Flow Flow. Press. Press. Press 15 4.200 21.00 21.00 0.00 2,5.000 Pt 25.000 0.000 21 9.200 21.20 2-1,Q0 0.20 25- 480 Pt 25.0:00 0.48-0 Total K Factors, 2 Totil Fixed Flows.. 0 Sum Actual Flow. 42.20 Sum Required Flow 42.00 Sum Delta Fl 1, 1 'QW 01.20 Max Delta Flow Max Delta Pressure- 0..4,80 AREA CALCULATED COMPLETE I SUMMARY Start Finish Diam. Start Normal Pf Elev/Fixed Flow vel Point Point Pres. Pres. Pres, 1'6 1- 101 25.0-00 0.359 -0. 4-33 21,0E 7.08 16 <_ 17 1,101 24.92.6 2.676 3. 967 21.00 7.08 17 <- 18 1.394 31.570 0. 169 .0.00o 21 .00 4.41 18 <- 19 1.394 31 .739 16. 1,32 6. 354 42.20 18.81 19 <- 20 1.265 54 .224 5.001 0. 000 42,20 10. 77 20 <- TOR 1.442 59-2215 13.515 -6. 354 42,20 8.29 TOR <- BOR 1. 61 56.386 0.943 6. 755 42.20 6. 65 BOR < UGI 1.610 64.084 0.001 14. 737 42,20. 6. 65 UG1 <- UG2 4.100 68.823 0. 025 2.599 42.20 1 .03 - UG2 < UG3 4. 100 71.446 0,057 0.000 42.20 1.03 UG3 < TEST 8.270 71.504 0.009 -2.165 42.20 0.25 21 <..- 22 1. 101 25, 480 0.-076 0.433 21.20 7.14 — 22 <- 23 1.101 25. 123 1 .805 3.9.67 21.20 7.14 23 <- 18 1. 101 30.895 0.844 0.000 21.20 7 .14 Pipe with highest velocity: 19 - 20 (10.773) Water Supply Summary 0 Point TEST Total. Flow From Water Supply Curve . . . . 42,201 Pressure From Water Supply Curve. .. 117.984 System Pressure Demand At. Supply Curve 69.347 Safety Margin at Supply Curve. 48636 — Y 2 i I j J J i J i 1 J Alk AM I Fire.Protection by Computer Design ENCORE FIRE PROTECTION 110 MURPHY ROAD HARTFORD CT 0611.4 7 S 8602467711 J Job Name 2-SPI-17005 BUILDING 3&4 CALC Drawing 3&4 Location 175 OAKLAND ROAD SOUTH WINDSOR CT 07074 Remote Area 1 Contract 2-SPI-17005 Data File 2-SPI-17005 BUILDING 3&4 CALC Area 1.WXF i J Computer Programs by Hydratec Inc. Route lil Windham N.H. USA 03087 ENCORE FIRE PROTECTION Page 1 BUILDING 3&4 CALC Date HYDRAULIC DESIGN INFORMATION SHEET Name - 175 OAKLAND ROAD Date - 1-31-2017 Location - 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Building - 3 & 9 System No. - 1 Contractor - ENCORE FIRE PROTECTION Contract No. - 2-SPI-17005 Calculated By - JA Drawing No. FP-3 Construction: (X) Combustible ( ) Non.-Combustible Ceiling Height 9'0" — OCCUPANCY - R'ESIDENTIAL S Type of Calculation: ( )NFPA 13 Residential (X)NFPA 13R (. )NFPA 13D Y Number of Sprinklers Flowing: ( )l ( )2 W 4 t ) S ( )Other T j )SPecific> Ruling Made by Date E` M Listed Flow at! Start Point 21- Gpm System Type: Listed Pres. at Start Point 15 Psi (X) Wet j ) Dry D MAXIMUM LISTED SPACING 16' x 181 4 ) Deluge j ) PreAction E Domestic Floor: Added - Gpm Sprinkler or, Nozzle S Additional F16w .Adde.d - Gpm. Make TYCO; Model LFII I Elevation .at Highest: Outlet - 18.83Feet Size 1/211 K-Factor 4.2' G Note: Temperature Rating 155 N Calcul.atLon Gpm RequiredB6.661 Psi Required 7.2,651 At Test. Summary C-Factor Used: Overhead. 150 Underground 150. W plater Flow Test Pump Data: Tank or Reservoir: A Date of Test - 1997 Rated Cap. Cap. T Time of 'Test - @ Psi Elev. ' E Static (Psi)' - 118 Elev. R Residual (Psi) - 58 Other Well Flow (Gpm) 1980' Proof Flow Gpm -r S' Eleyatioli 6 P Location: ;OAKLAND ROAD P L Source of Information, MDC HYDRANT FLO3 RECORDS Y I Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 . .. . . .. .. . . .. Water Supply Curve C ENCORE FIRE PROTECTION' BUILDING 3&4 CALC Page 2 Date City Water Supply; Demand; C1 -Static Pressure 118 D1-Elevation 7722 C2-`Res .Residual Pressure; 98 D2-.System Flow :87.72 C2-Residual Flow 1980 D2-'System,Pressure 72.651 Hose(Demand) D3-:System Demand : 86.661 Safety Margin 46.288 150 140 130 p 120 C9 ! R 110 E 100 S 90 S 80 D2 U 70 R 60 E 50 40 I 3.0 a 20 10 D1 I 200 400 600 800- 100.0 1200 1400 1600 1800 FLOW(N'"1..M Computer Programs by Hydratec Inc. Route l i 1 Windham N,M:USA fl3087 Fittings Used Summary Page 3 ENCORE FIRE PROTECTION Date BUILDING 3&4 CALC Fitting Legend f?_-__...._'/� 1 1'/. 1'%z 2 8 10 _..._.12 14 16 18 20 24 Abbrev. Name —— E NFPA 13 90'Standard Elbow 1 2 2 3 4 5 6 7 8 10 12 14 18 22 27' 35 40 45 50 61 Fsp Flow Switch Potter Fitting generates a Fixed Loss Based on Flow G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 T 8 91 11 13 T NFPA 13 90'Flow thr u Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Zaa Ames 2000B Fitting generates a Fixed Loss Based,on Flow Units 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 Nydratec Inc. Route II! Windham N,.H.USA 03087 Pressure / Flow Summary- STANDARD ENCORE FIRE PROTECTION Page 4 BUILDING 3&4.CALC , Date Node Elevation K-Fact Pt Pn Flow Density Area Press No.. Actual Actual 1 17.83 4.2 26.24 na 21.51 0.05 29 25.0 2 18.83 25.95 na 3 9.67 30.4 na -` 4 967 32.2 na 5 9.67 35.77 na 6 9.67 38.48 na TOR 9,67 53:99 na BOR 1.0 65.29 na UG1 1.6 71.99 na UG2 -6.0 74.6 3 na UG4 -5.0 74:78 na TEST 0,0 72.66 na 8 17,83 4.2 25.17 na 21.07 6.05 230 25:0 9` 18.83 25:1 na 10 17.83 4.2 25.0 na 21.0 0.05 221 25.0 11 10.83 24.93 na 12 17.83 4.2 30.18 tia 2307 0,05. 47 25:0 13, 18,83 30..18 na j i J The maximunn velocity is 1822 and it occurs in the pipe between nodes 6 and TOR { II I I i i I ' J Computer Programs by Hydratec Inc. Route 11'1 Windham N.H. USA 03087 Final Calculations Hazen-Williams - 2007 - ENCORE FIRE PROTECTION Page 5 BUILDING 3&4 CALL Date Node1 Elev1 K Qa Nom_ Fitting Pipe CFact Pt to or Ftng's Pe "****k* Notes * #*� Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 1 17.830 4.20 21.51 1.25 E 4.762 1.000 150 26.238 to 0.0 4.761 -0.433 2 18,830 21.51 1M4 0.0 5.761 0.0246 0.142 Vel= 4.52 2 18.830 _ 0.0 1.25 2E 9.523 10.080 150 ^ 25.947 to 0.0 9.523 3.967 3 9.670 .21.51 1.394 � 0.0 19.603 0,0247 0.484 Vel= 4.52 _ 3 9.670 21.08 1.25 2T 19.046 1.540 150 30.398 to 0.0 19.047 0.0 4 9,670 42.69 1.394 0.0 20.587 0 0873 1.797 Vel= 6.95 4 9.670 21.00 1.25 T 9.623. 9.980 150 32.195 to 0:0 9.523 0.0 - _5 9,670 63,59 1,394 0.0 19.503 0.1833 3,574 Vel= 13.37 5 9.670 0.0 1.25; 0.0 14.810 150 35.769 to 0.0 0.0 0.0 6 9.670 63M 1,394 _ 0.0 14.810 0.1833 2.714. Vel= 13.37 3 6 9.670 23.07 1.25 2E 9,523 38.200 150 3$.483 I to 0.0 9,523 0:0 TOR 9,670 86.66 _1.394 0.0 47.723 0.3249 15.506 Vel 18.22 TOR 9.670 6.0 1.5. E 4.0 14.670 120 53,089 to Fsp 0.0 4:000 6.755 '"Fixed Loss=3 -` BOR 1 86.66 161 0.0 18.670 0.2434 4.546 Vel.= 13.66 _ BOR 1 0.0 1:5 zaa 0.0 0.010 120 65.289 to O.o 0.0 6.700 Fixed Loss 6.7 UG1 1. 86.66 1.61 00 0.010� 0.300.0. 0.003 Vel= 13.66 _._...__ UG1 1 0.0 4 E 14.534 6,000 140 71.992 to 0.0 14,634 2.599 UG2 -5 86.66 4.1 0.0 20,534 0.0019 0.039 Veil= 2.11 UG2 -5 0.0 4 G 2.907' 45.000 140 74.630 _ to T 29.06:7 31.974 0.0 UG4 -5 86.66 4.1 0.0 76.974 0.0019 0.148 Vel= 2.11 UG4 -5 0.0 8 2G 12.652 480.0010 140 74.778 to 2E 56.936 124.942 -2.166 TEST 0 86.66 8.27 T 55.354. 604.942 0.0001 0,039 Vel= 0.52 0.0 TEST _ 86.66 _ �T 72.651 K Factor= 10,17 8 17.830 4.20 -2`1.07 1 E 3.825 1.000 150 25,174 to 0.0 3 825 -0,433 9 18:830 21.07 1.101 0.0 4.825 0.0750 0,362 Vel= 7:10 9 18.830 0.0 1 2E 7,65 %070 150 25,103 to 0.0 7.650 3.967 3 9.670 21.07 1.101.... 0.017.720 0,0749 1:328 _Vel=-7.10 ...._..... ._._...- -- -- _.... OA 3 _ 21.07 _ ----._. 30.398 K Factor= 3.82 10 17.830 4.20 ---21.00 1 E 3.825 1.000 150 25.000 to 0.0 3.825 -0.433 11 18.830 21.0 1.101 0.0 4.825 0.0744 0.359 Vel= 7.08 11 18,830 0.0 1 5E 19.125 25,210 150 24.926 to 0.0 19.126 3.967 4 9.670 21.0 1.101 0.0 44,336 0.0745 3.302 Vel= 7.08 Computer Programs by Hydratec Inc. Route 111 Windham N.H.USA 03087 _ Final Calculations Hazen-Williams ENCORE FIRE PROTECTION Page 6 BUILDING 3. &4 CALC Date Node1 Efev1 K _ Qa Nom Fitting Pipe CFact Pt to or Ftrig`s Pe ** : • oxar Node2 Elev2 Fact Qt Act Eqv: Ln, Total Pf/Ft p f Notes 0.0 4 21.00 32.195 K Factor= 3.70 12 17.830 4.20 23.07 1 E 3,825 1.000 1.50 30.183 to 0.0 3.825 -0.433 13 18.830 23.07 1.101 0.0 4.825 0.0887 0.428 Vel 7.77 13 18.830 0.0 1 2E _ 7,65 22.160 150 30.178 ^ to 2T 1.9.125 26.776 3.967 6 0.670 23.07 1.101 0.0 48.9.36 0.0886 4.338 Vel 7.77 0..0 _ 6 23.07 38.483 K Factor- 3,.72 f i �J I I i �f I i �J ,J i i J I Computer Programs by Hydratec Inc. ROtite 111 Windham N.H. USA 03087 General Calculation Program . Job - BUILDING 3 & 4 CALC Date 02/03/17 File - C:\HES\HydraCALC\Ver50\Data\Jobs\2-SPI-17005 BUILDING 3 & 4 CALC Area. l.WXFTime - .13i27:22 AREA CALCULATED- HEAD FLOW SUMMARY Actual Req. Delta Actual Req. Delta. ID K-Factor Flow Flow Flow- Press. Press. r Press 1 4..200 21.51 21.00 0.51 26.238 Pt 25.000 1.236 8 4.200 21.07 21.00 0.03 2`5.17'4 Pt 25.0.00 0.174 10 4.2.00 21.00 21:00 0.00 25.000 Pt 25.600 0.000 12 4.2.00 23.07 21.00 2.07 30.183 Pt 25.000 5.183 Total K Factors. 4 Total Fixed Flows:. . 0 Sum Actual Flow. $6.6.6 _ Sum Required Flow. 84.00 Sum Delta Flow 2.66 Max Delta Flow 2.07` Masi Delta Pressure 5.183 AREA CALCULATED COMPLETE SUMMARY start Finish D-iam, Start Normal Pf Elev/Fixed Flow Vel Point Point Pres. Pres Pres. 1 <- 2 1 .394 26.2H 0.142 -0.433 21 .51 4.52 2 <- 3 1 .3.9.4 25.947 0.484 3:9'67 21 .51. 4.52 3 <- 4 1. 394 30.398 1 .797 MOO 42.59 8 .95 4 <-• 5 1 ,394 32. 1.9 3.574 0.000 63.59 1.3. 37 5 6 1.394 31).'169 G. 11 4 U.0.U0 63, 59 13.37 r 15.506 0.000 6 <- TOR 1 .394 38 .483 86.66 18.22 TOR <- BOR 1.610 53.989 4.545 6.755 1 86. 66 13. 66 BOR <- UG1 1.610 65.289 0.002 6.70.0 86. 66 13. 66 UGl <- UG2 4. 100 71, 992 86. 66 2. 11 0.040 2.-599 UG2 <- UG4 4. 100 74. 630 .0.149 0.000 86.66 2.11 UG4 <- TEST 8.270 74.778 0.038 -2.165 86.6,E 0.52 8 <` 9 1.101 25.174 0.362 -0.433 21.07 7. 10 9 3 1.101 25.103 1.329 3.967 21..07 7. 10 10 <` 11 1. 101 25.00.0 0.359 -0. 433 21.00 7.0.8 11 <`- 4 1,101 24.926 3.302 3,967 21.00 7.08 12 <- 13 1.101 30.183. 0°.42.& -0.433 23.01 7,79, 13 <- 6 1.101 30..178 23.07 7, 78 4.338' 3.967 J pipe wi�h highest velocity:, 6 - -TOR (18.217) Water Supply Summary `C� Point TEST J Total Flow From Water _Supply Curve Pressure From Water Supply Curve . .. 117 939 System Pressure Cemand: At Supply Curve . Safety Margin at Supply Curve _ 72.651 45.28.$ J - j i � F J 2 i J J I �J i {}II I i �l . Fire Protection by Computer Design ENCORE FIRE PROTECTION 110MURPHY ROAD ; Chu HARTFORD CT 06114 8602467711 i Job Name 2-SPI-17005 BUILDINGS 5&6 CALC _ Drawing 5&6 Location 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Remote Area 1 Contract 2-SPI-17005 Data Fite 2-SPI-17005 BUILDINGS 5&6 CALC Area 1.WXF Computer Programs by Hydratec Inc. Route ill Windham N.H. USA 03087 ENCORE FIRE PROTECTION Page 1 2-SPI-17005 BUILDINGS 5&6 CALC Date HYDRAULIC DESIGN INFORMATION SHEET - Mame 175 OAKLAND ROAD Date - 1-31-2017 Location - 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Building - 5 & 6 System No. - 1 Contractor- ENCORE FIRE PROTECTION Contract No.. - 2-SPI-17005 Calculated By - JA Drawing. No. - FP-5. Construction: M Combustible ( ) Non-Combustible Ceiling Height. 9''0" OCCUPANCY - RESIDENTIAL S Type of Calculation: ( )NFPA 13 Residential (X):NFPA 13R ( )NFPA 13D Y dumber of Sprinklers Flowing: ( ):1 f )2 (X)4 ( ) S ( )Other T ( )Specific Ruling Made by Date: E M Listed Flog at Start- Point - 21 Gpm System Type J Listed Pres. at Start. Point - 25 Psi M Wet ( ) Dry D MAXIMUM LISTED SPACING 16, x Is, ( ) Deluge,. ( ) PreAction E Domestic .Flow Added; - Gpm Sprinkler or Nozzle S Additional Flosi- Added: Gpm Make TYCO Model LFII, I Elevation at Highest Outlet - 18- 83Fee't Size 1/:2" K-Factor 4.2' G Note: Temperature Rating' 155. N Caalculation Gpm Required 93.008 Psi Required 109.657 At Test Summary C-Factor Used: Overhead 186,, Underground 150 j W 110er Flow Test:; Pump Data: Tank or Reservoir: A Date: of Test 1997 Rated Cap, Cap: T Time- of Test - 0 Psi Elev. E Static (Psi.:) - 118 Eleu:. R: Residual (Psi): - 98 Other Well Floc; ('Gpm) - 1980 .Proof Floss Gpm: S' Elevation 0 P Location: OAKLAN;D ROAD P L Source of Information: MDC HYDRANT FLOW RECORDS 1 Y f Computer Programs by Hydratec Inc. Route'II I Windham N,H. USA 03087 1 -__-- L L.___ 1_ i_ ._.- � t �__-- t L ------ L L t 1------- Water Supply Curve C ENCORE FIRE PROTECTION Page 2 2-SPI-17005 BUILDINGS 5&5 CALC Date City Water Supply: Demand:; C1 -Static Pressure : 118 D1 -Elevation 8.155 C2-Residual Pressure: 98 D2-System Flow : 93.008 C2-Residual Flow 1980 D2-System Pressure : 109.657 Hose( Demand) Da-System Demand, :93.008 Safety Margin 8.273 150 140 130 P 120 C1 D2 i R 11.0 E 100 S 90 S 80 U 70 R'60 E 50 i 40 , 30 20 10 D1 200 400 600 300 100.0 1200 1400 1600. 1800 FLOW(N^ 1,85') Computer Programs by'Hydratec Inc. Route. 111 Windham N.H. USA 03087 Fittings Used Summary ENCORE FIRE PROTECTION Page 3 2-SPI-17005 BUILDINGS 5&6 CALC Date Fitting Legend 2 2'/ 3 3%Z 4 5 6' 8 10 12 14 16 13 20 24_ Abbrey. Name % .. 1 1'1, 1'/z ' E NFPA 13 90'Standard ElC} vd 2 2 3 4 5 fi 7 8 10 12 14 18 22 27 35 40 45 50 61 Fsp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow 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 Zaa Ames 2000B Fitting generates a Fixed Loss Based on Flow Units 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 b,y manufacturers based on specific pipe diameters and CFactors and they requ re'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. Route 111 Windham N.H.USA 03087 Pressure / Flow Summary -STANDARD j ENCORE FIRE PROTECTION Page 4 2-SPI-17005 BUILDINGS 5&6 CALC Date Node Elevation K-Fact Pt Pn Flow Density Area Press No. _ - Achiai Actual Reg. 1 18.83 4.2 25.0 na 21.0 0.05 215 25.0 2 18.83 25.65 na: 3 9.67 38:33 na 4 9.67 50.7 na 5 9.67 52.46 na 6 9.67 73.39 na _ 7 1.0 81.39; na 8 9.67 85:14 na 9 6.67 8819 na TOR' 0.67 86.62 na BOR 1.0 161.66 na J UG1 1.0 108.97' na UG2 -5.0 111.61 na UG6 -5.0 111.8 na. TEST 0:0 10 .66 na _ 13 18.83 4.2 25.02 na 21.01 o05 41 9.6 14 t8.8:3 4.2 31.55 na 2159 0.05 208 25.0 i 15 18.8.3 4.2 42.58 na 27.41 0.05 46. 16.4 9.07 50.12' - na J � i The maxirnum velocity is 22.11 and it occurs in the pipe between nodes 3 and 4 J I i f �.. f J I E i i .JJ j J i i J i J i. i �J Computer Programs by Hydratec Inc. Route 111 Windham N.H.USA 03087 Final Calculations - Hazen-Williams -2007 ENCORE FIRE PROTECTION Page 5 2-SPI-17005 BUILDINGS 5&6 CALC Date Node1 Elev1 K Qa Nom Fitting Pipe CFact = Pt Pe Notes *k '* to or Ftng's Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 1 18.830 4.20 21.00 1 2E 7.66 1.125 150 25.000 - to 0.0 7.650 0.0 2 18.830 21.0 1.101 _ 0.0 8.775 0.0745 -0.654 Vel a= 7.08 2 - ` 18.830-_ - 21.01�-1 2T 19.125 13..292 160 25.654 to 0.0 19- 26 3.967 3 9.67 42.01 1.101 0.0 32.418 0.2686 8.706 Vel 14:16 3 9.67 23.59 1 T 9.563 10..64.0 150 38.327 to 0.0 9.562 0.0 4 9.67 65.6 1.1.01_ 0.0 20.202 0.6126 12.375 Vel= 22.11 4 9.6T 0.0 1.5 0.0 17.660 150 50.702 0 0.0 0.0 5 9.67 65.6 4.698 0.0 1,7.660 0:0998 1.762 Vel= 10:49. 5 9.67 27.41 1.6 4T 46:624. 57.440 150 52A64 as E 5828 52.452 0.0 6 9.67 93.01 1.698 0.0 109.802. 0.1904. 20.926 Vet= 14.88: 6 9.67 0 0 1.6 2E 9.9 8.670 120 73.390 to 0.0 9.900 3.755 7 1 93.01 1:6;82 0,0 1`8.570 0;2242 4.163 Vel= 13.43 7 0,0 1.5 0 0 29.750 160 81.30.8 to 0.0 0.0 3.756 8 9.670 93.01 1.505 0.0 29.750 0.2550 7.686 Vet= 16.77 8 9,670 00 1.5 E 495 8.667 120 85.139 to 0.0 4.950 0.0 9 9.670_ _ 93:01 1 M2 0.0 13.617 0<2242 3.053 Vel.= 13.43 9. 9,670 0.0 1.5 0.0 1.910 120 80:O9 2 fa 0.0 0.0 FOR 9 676 03.01 1.682 0.0 1.91t7 0:224T 0.42$ Val= 13:43 TOR 9.670 0:0 1.5 2E 8.0 14.670 120 88.620 to Fsp 0.0 8:000 6.755 *'*Fixed Loss=3 BOR 1 9101 1.61 00 22.670 Q2775' 6.290 1let= 14.66 - BOR 1 0.0 1.5 Zaa 0.0 0.010 120 101.866 to 0.0 0,0 7.300 *Fixed Loss= 7.3 UG1_ 1 _93.01_1.61 0.0 _ 0.010 0:3000 0.003 Vel= 14.66 V UG1 1 :0.0 4 E 14.5.34 6.000 14.0 108.968 to 0.0 14.534 2.599 UG2 -5 9.3.01 4_1�_..- -- ---0.0 ...__..20.534 --0.0022-- 0.045 Vel= 2.26 _ - -------- UG2 -5 0.0 4 E 14.534 70.000 140 111.612 to 0.0 14,534 0.0 UG6 -5 93.01 4.1 0.0. 84.534 0.0022� 0.186 Vel= 2.25 _ --------._-. - UGE� -__---- ---- -- 0.0 8 0..0 345.000 140 111.798 to 0.0 0.0 -2.166 - _ 0.0 3Q5`0a0�- 0,000.1 0.025 Vel- 0_56 TEST 0 93A1 8.27 -- - -,-�--- OA 109.657: 1<Factor= 8:88 TEST 93.01 13 18.83 4.20 21.01 1 2E 7.65 0.833 150 25.021 to 0.0 7.6.50 0.0 2 18.830 21.01 1.101 0.0 8.483 0..0746 0.633 Vel= 7;08 0.0 computer programs by Hydratec Inc. Route-111. Windham.M.H..USA 03087 Final Calculations - Hazen-Williams ENCORE FIRE PROTECTION Page 6 2-SPI-17005 BUILDINGS 5&6 CALC Date Node1 Elev1 ,K Qa Norn Fitting Pipe CFact Pt to or Ftng's Pe **** t. Notes * Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft . Pf 2 21.01__ 25.654 K Factor 4.15 14 18.83. 4.20 23.59 1 2E 7.65 22.780 150 31.550 to 0.0 7.650 3,967 3 9,67 23.59 1.101 0.0 30A30 0.0923 2.810 Mel= 7.96 0,0 3 23 59 38.327 K Factor 3.81 15 18.8.3 4.20 27.41 1 2E 7.65 12.060 150. 42.584 to T 9.563 17.212 3.067 16 9.67 27 41 1.101 0.0 29.272 0,1219 3.568 Vel= 9.24 16 9,67 0;0 1 T 9.56:3 9.680 150: 50.119` to 0.0 9.502 off 5 9.67 27.41 1,101 0.0 19.242 0,1219 2.345 Vel- 9.24 00 5 27.41 52:464 K Factor= 3.78 i I J I i �I I i J i J Computer Programs by Hydratec►nc. Route 1'11 Windham N.H.USA 03087 General Calculation Program Job - 2.-SPI-17005 BUILDINGS 5 & 6 CALL Date 02/03/17 File - C:\HES\HydraCALC\Vpr50\Data\Job5\2-SPI-17005 BUILDINGS 5 & 6 CALC: Area l.WXFTime - 13:34:35 AREA CALCULATED - HEAD FLOW SUMMARY Actual Req. Delta Actual Req. Delta ID K-Factor Flow Flow Flow. Press- Press. Press 1 4.200, 21,00 2 1 0.0 0.00 25.000 Pt 25.000 O.Ho 13 4,200 21.01 13.01 8.00 25.021 Pt 9.GOO 15. 421 14, 4.200 23.59 21.00 L 59 31-5. 49 Pt 25.000 6.54.9 15: 4.2010 27.41- 171.01 10.40 4 2.5.8 4 Pt 16.40.0 26.184 Total K Fa,ctors, 4 Total Fixed Flows. . . 0 Sum Actual Flow. -q3 0 1 Sum Requit-ed Floor; 72.02 Sum Delta Flow 201.99 Max Delta Flow 10.40, Max Delta Pressure- 26 1 8A AREA CALCULATED - COMPLETE SUMMARY Start Finish, Diam. Start Normal Pf Elev/Fixed Flow Vel Point Point Pres. Pres. Pres, 1 2 1 .101 25..0.00 0.653 0A00 21 .00 7 .08 2 <- 3 1 . 101 25,653 8 .706 3. 9,67 42.01 14 . 16 3 <- 4 1 . 101 38 .327 12.375 0,000 65.60 22. 11 4 5 1 .55,81 50.702 1.763 0.000 65. 60 :1.0,49 5 6 i.598 52. ,164 ;,?0.926 0.000 93.01 14 .88 6 <- 7 1,682 73. 39-0 4 .163 3.755 93.01 13.43 7 <- 8 1 .505 81.308 7.586 -3.755 J 93.01 16.77 8 <- 9 1. 682 85. 139 3.053 0.000 93.01 13.43 9 <- TOR 1. 682 88,192 0.429 0.000 93. 01 13.43 _ TOR <- BOR 1. 610 88. 621 6..290 6.155 98.01 14.66 BOR <- UGl 1. 61,0 101.665 0.003 7.300 93..01 14>66 UG1 <- U62 4: 100 108.968 0..0.45 2.599 93..01 2.26 UG2 <- UG6 4.100 111..612 0.186 0.000 93.01 2.26 UG6 < TEST 8.270 111.798 0.025- -2.165 93.01. 0.56 13 < 2 1. 101 25.021 0..632 0.0:00 01 7,08 14 < 3 1. 101 31..549 2.$'10 3.967 21.5 9 7 95 f. 15 <- 16 i.101 42.58`4 3.5,683 9V 27.41 9..24 16 <- 5 1.1,01 50. 119+ 2.345 0.000 27.91 9.24 i Pipe with highest velocity 3 - 4 (22.106) water Supply Summary @ Point TEST i Total Floe From: Water Supply Curve 93.008 Pressure From Wager Supply Curve 117.93.0 System Pressure Demand At Supply Curve 109.657 j Safety Margin at Supply Curve. $.273 } _.i i J ' z _I i i i - _I I J J I - Fire Protection by Computer Design < � I -- 0 ttG: }0.00013 ENCORE FIRE PROTECTION f r . 110`MURPHY ROAD j HARTFORD CT 00114 J 8602467711 i Job Name BUILDING 7 CALC Drawing 7 Location 175 OAKLAND ROAM SOUTH WINDSOR CT 06074 Remote Area : 1 Contract : 2-SPI-17005 Data File 2-SPI-17005 BUILDING 7 CALC Area 1.WXF f 4 i J Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 . i ENCORE FIRE PROTECTION Page 1 BUILDING 7 CALC Date HYDRAULIC DESIGN INFORMATION SHEET _ Name 17.5 OAKLAND ROAD Date - 1-31-2017 Location - 175 OAKLAND ROAD SOUTH WINDSOR CT 06074 Building - 7 System tlo. - `1 Contractor - ENCORE FIRE PROTECTION Contract No. 2-SPI-17005 Calculated By - JA Drawing No. -, FP-6 Construction:; (X) Combustible ( ) Non-combustible Ceiling Height 91011 OCCUPANCY -- RESIDENTIAL S Type of Calculation: ( )NFPA 13: Reside.ntia'l (X)NFPA 13R ( )"NFPA 131) �- Y Number of Sprinklers Flowing ( )1 ( )2 (X_)4 S ( )Other T (. )Specific Ruling Made by Date M Listed Flow at Start Point - 21 Gpm System Type Listed Pres. at Start Point - 25. Psi (X) We.t { ) Dry D MAXIMUDf LISTED SPACING 16, x 18' ( ) Deluge ( ) PreAction E' Domestic Flow Added - Gpm Sprinkler or Nozzle S Additional Flow Added Gpm; Make TYCO Model LFTI I Elevation at Highest nutlet - 18.83Feet Size 1/2" K=Factor 4.2. G Notet Temperature Rating '155 N f Calculation Gpm Required 85.796 Psi Required 64.09..4 At Test SumsnarJ C-Factor Used,: Overhead 15P Underground 150 W' Plater Flow Test,. Pump Data': Tank or Reservoirs A Date af. Test - 1997 Rated Cap. Cap. T Time. of Test @ Psi Elev, E. Static (Psi) - 11:8 Eiev•. 8 Residual ('Psi) 98 'Other W611 Flow ('Gpm:) - 19.80 ptbof Flow Gpm. _ S Elevation - '0 _ P: Location; OA L.AND ROAD P L Source of Information: MDC HYDRAIIT FLOP] RECORDS Y i f i Computer Programs by Hydratec Inc. .Route 1 I Windham N.H.USA 03087 _ il-- Water Supply Curve C ENCORE FIRE PROTECTION Page 2 BUILDING 7 CALC Date City Water Supply: Demand: C1 Static Pressure 113 . D1 Elevationn 8155 C2-Residual Pressure: 98 D2-:System :88.155 C2-Residual Flow 19$0 D2-System Pressure s 64.094 Hose(Demand) D3'-System Demand .85.796 Safety Margin 53.846 150 140 1$0 p 120 C1 R 11.0 E. 100 S 90 S 80 j U 70 ! R 60 E 50 s 40 I 30 20 10 D1 200 400 600 800 1000 120G 1400 1600 1800 FLOW(N"1:85}' Computer Programs.byHydratec Inc. Route 111 Windham N.H,USA 03067 Fittings Used Summary ENCORE FIRE PROTECTION Page 3 Date: BUILDING 7 CALC Fitting Legend 1 _..._._..._ ...__ . °/::___..3/ 1 1'/4 '/z 2 214 3 33,/24 5: 6 8 10 12 14 16 1 ._ 20 24 Abbrev: Name --- E NFPA 13 90'Standard Elb,^w 1 2 2 3 4 5 6 7 8 10 1.2. 14 18 22 27 35 40 45 50 61 Fsp Flow Switch PotterVSP, Fitting generates a Fixed Loss Based on Flow G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2. 3, 4 5 6 Z 8 10 11 13 T NFPA 13 90'Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 3.5 50 60 71 81 91 101 121 2aa Ames 20003 Fitting generates a Fixed Loss Based on Flow Units 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 basad or,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. Route;111 Windham N.H.USA 03087 ............ Pressure 1 Flow Summary- STANDARD ENCORE FIRE PROTECTION page 4 BUILDING 7 CALC Date Node Elevation K-Fact Pt Pn Flow No. Density Area Press Actual Actual _... Reg. 1 18,83 4:2 25.16 na. 21.07 0.05 45 25,0 2 18.83 25.39 na 3 9.67 31V na _ 4 9:67 32A4 na 5 9.67 35.58 na TOR 9:67 46.61 no BOR 10 56:87 na. UG1 1.0 63.48 na UG2 -6.0 86:11 na TEST 0.0 64.09 na J8 18.83. 4.2 25.6 na 21.0 0.05 230 26A 18.83 4.2 26.0 na 21.41 0,05 90 10 9.67 25:.0 3192 na 11 9.67 35.11; na 12 9.67 34.64 na 13 18.83 4.2. 28.23 na 22.32. 0:05 53 25:0 i The.maximum velocity is 18.04 and it occurs in the pipe between nodes 5 and TOR t J J { j I I i i j I i i i J Computer Programs.by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams - 2007 ENCORE FIRE PROTECTION Page _ 5 BUILDING 7 CALC Date Node1 Elev1 K Qa Note Eittng Pipe CFact Pt to or Ftng's Pe Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf 1 18.83 4.20 21.07 1.25 T 9.523 0.180 150 25.166 to 0;0 9.523 - 0.0 2 18.83 21.07 1.394 00. 9.703 0.0237 0.230 Vel= 4.43 2 18.83 21.00 1.25 2E 9.523 10.610 1,60 25.388 to 0.0 9.523 3.967 3 9,67 42.07 1.394 0.0 20.133' 0.0853 1.718 Vet.= 8.84 3 9.67 Q0 1.25 T. 9.523 3.060 150 31.071 to 0.0 9.523 0.0 4 9,67 42.07 1.394 0.0 12.583 0.0854 1.074 Vol;= 8.84 4 9.67 21.41 1.25 T 9.523 9.270 150 32.145. to 0.6 9.523 0.0 _ 5 9.61 61,8 1..3- 0.0, 18.793' 0A 827 3.433` Vet= 13.34 5 9.67 22.32 1.25 T 9.523 15.550 150 35.578 to 2E 9.523 19046 0.4 TOR 9.67 85.8 1394 0.0 34.596 0.3189 11.034 Vel- 18.04 _ -r TOR 9.67 0.0 15 Fsp 0.0 14.670 120 46.612 to 0.0 0.0 6.755` "' Fixed Loss=3 BOR 1 85:8 1.61 0.0 14.670 0.2390 3.506 vol.= 13.52 BOR 1 0.0 1.5 Zaa 0':0 0.010 120' S6.873 to 0.0 0.0 6.600 Fixed Loss=6.6 UG1 1 85 8. 1.61 0 0 0.010 0 2000 0.002 Vef= 13.52 UG1 1 0.0 4 E 14;534 6.000 140 63.475 to 0 0 14.534 2.590 UG2 -5 85:8 4.1 0.0 20.534 0.001'9 0.038 V61= 2.09 UG2 -5 00 4 E 14534 60.000 140 66.112 to G 2'.907 1.7.441 -2.166 t TEST 0 858 4:1 00 77.441 0;0019 0.148 Vet= 2.09' 00 TEST g5g0 64.094 K Factor= 10.72 8 18.83 4:20. 21 A0 1 E 3:825 1..360 150 25.000 to 0.0 3.825 0.0 2 18.8321,0 1,101 0.0 5.185 060744 0.386 Vel= 7.08 0.0 2 2100_ 25386 K Factor- 4.17 9 18.83 4.20 21.41 1 3E 11A75 13.930 150 25.996 to 0-0 11,475 3.967 10 9.67 21.41 1.161 0.0 25.406 0.0772 1.961 _ „Vel= 7.21 10 . 9.67 0.0 1.25 0.0 9.000 150 31,924 - to 0.0 0 0 0.0 4 9.67 _ . 21_41 1.394 0.0 „ 9,000 0.0246. 0.221. _Vel= 4.50 0.0 4 21..49 _ 32.145- t4 Factor=`378 ........... -- ------ - 5 9.67 -22.32 1.25 0.0 17.660 150 35.578 to 0.0 0.0 0.0 11 9.67 -22.32 1.394 0.0 17.660 .0.0264 -0.467 Vel= 4.69 - 11 9.67 0.0 1.25 T 9.523 8.310 150 35111 to 0.0 9.523 0.0 12 9.67 -22.32 1.394 0.0 17.833 -0.0264 -0.471 Vet= 4.69 Computer Programs by Hydratec Inc. Route ill. Windham N.H. U.SA 03087 - —� Final Calculations -Hazen-Williams ENCORE FIRE PROTECTION Page 6 BUILDING 7 CALC Date J Node1 Elev1 K Qa Norn Fitting Pipe CFact Pt to or Ftng's Pe **`***" Notes ***** Node2 Elev2 Fact Qt Act Eqv. Ln. Total PfIrt Pf 0.0 1.2 -2232 34.640: K Factor= -3.79 13 18,83 4.20 22..32 1 2E 7.65 12.090 150 28.232 _ to T 9.563 17.212 3.967 12 9.67 2232 1.101 0.0 29.302 0.0833 2.44.1 Vel= 752 0.0 12 22.32 34.840 K.Factor= .3.79 i �.i 4 k i J -- Coniptiter Programs by Hydratec Inc. Route 111 Windham N.H.USA 03087 General Calculation Program Job - BUILDING 7 CALC Date 02/03/17 File C:\HES\HydraCALC\Ver.50\Data\Jobs\2-SPI-1.7005 BUILDING 7 OALC Area 1.WXFTime - 13:39:33 AREA CALCULATED - HEAD FLOW SUMMARY Actual Req. Delta Actual Req. Delta ID K-Factor Flow Flow Flow. Press Press. Press 1 4.200 21.07 21.00 0.07 25.156 Pt 25.000 0.156 8 4.200 21.0Q 21.00 0.00 25.G00 Pt 25.000 0.000. 9 4 .200, 21.41 21.00 0.41 25.996 Pt 25.000 0.396 13 4 .2.00` 22.32 21.00 1.32 28.2.32 Pt 25.000 3.232 Total K 'Fact'ors. 4 Total Fixed Flows. 0 Sum Actual Flow. 85.80 Sum Required. FloW. . 84.GO T Sum Delta Flow. . 1.80 Max- Delta Flow 1.32' Max Delta Pressure 3.232 AREA CALCULATED - COMPLETE SUMMARY Start Finish Diam. Start Normal Pf` ElevlFixed Flow Vel Point Point Pres. Pre;s, Pres. 1 <- 2 1.394 25.15.6 0.230 0.000 21.07 4 . 43 2 <- 3 1.394 25.386 1.718 3.967 42.07 8 ,84 3 <-- 4 1..394 31.071 1 , 074 0.000 42.07 8.84 4- <- 5 1.394 32.1,45 3. 433 0.000 03. 48 13. 34 i <- TOR 1.394 35.5/8 11.034 0.000 85.80 1.8 .04 TOR <-- DOR 1.610 10 46.612 3. 506 6.75`5 85.80 13. 52 BOR <- UG1 1.610 56.873 0.002 6:.600. } t 1 i 85.80 13.52 UG1 <- UG2 4. 100 63.475 0.039 2,590 -� 8.5.80 2.0.8 UG2 <- TEST 4. 100 66.112 0.147 -2.165 85.80 2.08 8 < 2 1.101 25,1.000 0.386 0.000 21.00 7,08 9 <- 10 1. 101 25.996 1.1961 3.967 21.41 7.22 10 <- 4. 1.394 31.925: 0.220 0.000 21.Al 4.50 5 �> 11 1...39:4 35.578 -0.466 I } 0.000 -22.32 -4. 69. J 11 - 12 1 ,394` 35.111 0.471 0.000 -22,32 -4. 69 13 <- 12 1._101 28.232 2,442 3.967 I. 22.32. 7,52 Pipe with highest velocity- 5 TOR (18.0.36) Plater Supply Summary @ Point TEST 7 Total Flow From Water .Supply Curve 85.79E Pressure Prom Water supply Curvy 117`,940 System Pressure Demand At Supply Curve- 6.4.094 Safety Margin a Supp3y Curve. . 53. 8;46 i I j i i i J 1 J J f 2 i