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200 Deming Street - Building Plans & Dra
Q <Y 1 OG - - - Fire Protection by Computer Design y ,� LIC.P30.CM1 .? .nb'Of 9ti ALLSTATE FIRE SYSTEMS 110 MURPHY RD HARTFORD, CT. 06114 860-246-7711 Job Name THE RESIDENCE AT WINDSOR FARMS Building 3RD FLOOR RM 326 Location 200 DEMING STREET SOUTH WINDSOR, CT. System 1 Contract Data File RES CALC AREA 1.wxf ALLSTATE FIRE SYSTEMS Page 1 THE RESIDENCE AT WINDSOR FARMS Date Hydraulic Design Information Sheet Name - THE RESIDENCE AT WINDSOR FARMS Date - 10/15/13 Location - 200 DEMING STREET SOUTH WINDSOR, CT. Building - 3RD FLOOR RM 326 System No. - 1 Contractor - ALLSTATE FIRE SYSTEMS Contract No. - Calculated By - PAUL FORAUER Drawing No. - FP-3 Construction: ( ) Combustible (X) Non-Combustible Ceiling Height - 810 Occupancy - LIGHT HAZARD S (X) NFPA 13 (X) Lt.- Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure Curve S Other T Specific Ruling Made By Date E M Area of Sprinkler Operation - 650 System Type Sprinkler/Nozzle Density - .10 (X) Wet Make TYCO D Area Per Sprinkler - 252 ( ) Dry Model LFII E Elevation at Highest Outlet - 31 ( ) Deluge Size 1/2" S Hose Allowance - Inside - ( ) Preaction K-Factor 4. 9 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.160 G Hose Allowance - Outside - 100 N Note Calculation Flow Required - 202.433 Press Required - 73.077 Summary C-Factor Used: 150 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - 06/06/13 Cap. - T Time of Test - Rated Cap.- Elev.- E Static Press - 90 @ Press - R Residual Press - 70 Elev. - Well Flow - 2176 Proof Flow S Elevation - 0 U P Location - 200 DEMING STREET P L Source of Information - CONTRACT DRAWING FP0.00 Y C Commodity Class Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled % Palletized % Rack M ( ) Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Enca 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 G E Horizontal Barriers Provided: Hater Supply Curve (C) �LLSTATE FIRE SYSTEMS Page 2 "HE RESIDENCE AT WINDSOR FARMS Date City Water Supply: Demand: C1 -Static Pressure : 90 D1 - Elevation 13.426 C2 - Residual Pressure: 70 D2 -System Flow 102.433 C2- Residual Flow 2176 D2 -System Pressure 73.077 Hose ( Demand ) 100 D3-System Demand 202.433 Safety Margin 16.676 150 140 ' 130 P 120 R 110 E 100 C1 S 90 S 80 D2 U 70 C2 D R 60 E 50 40 30 20 10 300 600 900 1200 1500 1800 2100 2400 2700 FLOW( N ^ 1.85 ) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 ittings Used Summary LLSTATE FIRE SYSTEMS Page 3 HE RESIDENCE AT WINDSOR FARMS Date itting Legend bbrev. Name '/ % 1 14 1'/2 2 2'/ 3 3'/2 4 5 6 8 10 12 14 16 18 20 24 NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 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 sp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 '3 4 5 6 7 8 10 11 13 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 'ib Wilkins 350A Fitting generates a Fixed Loss Based on Flow Jnits Summary )iameter Units Inches .ength Units Feet -'low Units US Gallons per Minute 'ressure Units Pounds per Square Inch Jote: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. :quivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors �f 120 except as noted with *. The fittings marked with a *show equivalent lengths values upplied 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 :)r 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 ALLSTATE FIRE SYSTEMS Page 4 THE RESIDENCE AT WINDSOR FARMS Date Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Reg. 1 31.0 4.9 26.45 na 25.2 0.1 252 7.0 2 32.5 26.95 na 3 32.5 32.29 na 4 32.5 42.02 na 29 32.5 42.2 na 30 32.5 42.36 na 31 32.5 42.76 na 32 32.5 43.39 na 32A 32.5 45.86 na R2 32.5 49.85 na R1 9.5 59.84 na 5 9.5 59.86 na 6 9.5 59.89 na TOR 9.5 60.03 na BOR 1.0 66.77 na UG1 1.0 72.39 na UG2 -5.0 75.04 na UG3 -5.0 75.18 na TEST 0.0 73.08 na 100.0 8 31.0 4.9 25.66 na 24.82 0.1 170 7.0 9 32.5 25.17 na 10 32.5 25.72 na 11 31.0 4.9 25.26 na 24.63 0.1 138 7.0 12 31.0 4.9 32.14 na 27.78 0.1 253 7.0 13 32.5 31.68 na 36 32.5 42.36 na 21 32.5 42.5 na 21A 32.5 46.05 na R4 32.5 49.67 na R3 9.5 59.66 na 14 9.5 59.68 na The maximum velocity is 21.53 and it occurs in the pipe between nodes 3 and 4 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 5 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 1 25.20 1.101 IT 9.563 1.500 26.449 K Factor=4.90 to 150.0 0.0 9.562 -0.650 2 25.2 0.1044 0.0 11.062 1.155 Vel = 8.49 2 49.45 1.394 1 E 4.762 16.880 26.954 to 150.0 0.0 4.761 0.0 3 74.65 0.2466 0.0 21.641 5.336 Vel = 15.69 3 27.78 1.394 IT 9.523 12.460 32.290 to 150.0 0.0 9.523 0.0 4 102.43 0.4427 0.0 21.983 9.732 Vel = 21.53 4 -49.75 2.003 0.0 8.080 42.022 to 150.0 0.0 0.0 0.0 29 52.68 0.0222 0.0 8.080 0.179 Vel = 5.36 29 0.0 2.003 0.0 7.190 42.201 to 150.0 0.0 0.0 0.0 30 52.68 0.0221 0.0 7.190 0.159 Vel = 5.36 30 0.0 2.003 0.0 18.190 42.360 to 150.0 0.0 0.0 0.0 31 52.68 0.0221 0.0 18.190 0.402 Vel = 5.36 31 0.0 2.003 1 E 6.482 9.090 42.762 to 150.0 IT 12.965 19.447 0.0 32 52.68 0.0221 0.0 28.537 0.632 Vel = 5.36 32 0.0 2.003 IT 12.965 91.758 43.394 to 150.0 1 E 6.482 19.447 0.0 32A 52.68 0.0221 0.0 111.205 2.462 Vel = 5.36 32A 0.0 2.157 2E 12.307 10.542 45.856 to 120.0 IT 12.307 31.998 3.000 * Fixed loss = 3 R2 52.68 0.0233 1 B 7.384 42.540 0.992 Vel = 4.63 1 Fsp 0.0 R2 0.0 4.26 1 E 13.167 23.000 49.848 to 120.0 0.0 13.167 9.961 R1 52.68 0.0009 0.0 36.167 0.031 Vel = 1.19 R1 0.0 4.26 IT 26.334 0.500 59.840 to 120.0 0.0 26.334 0.0 5 52.68 0.0009 0.0 26.834 0.023 Vel = 1.19 5 5.74 4.26 IT 26.334 2.360 59.863 to 120.0 0.0 26.334 0.0 6 58.42 0.0010 0.0 28.694 0.030 Vel = 1.32 6 44.01 4.26 1 E 13.167 33.260 59.893 to 120.0 0.0 13.167 0.0 TOR 102.43 0.0029 0.0 46.427 0.135 Vel = 2.31 TOR 0.0 4.26 1 E 13.167 8.500 60.028 to 120.0 1 Fsp 0.0 13.167 6.681 * Fixed loss = 3 BOR 102.43 0.0029 0.0 21.667 0.063 Vel = 2.31 BOR 0.0 4.26 1Zib 0.0 0.010 66.772 to 120.0 0.0 0.0 5.616 * Fixed loss = 5.616 UG1 102.43 0.0 0.0 0.010 0.0 Vel = 2.31 UG 1 0.0 4.1 1 E 14.534 6.000 72.388 to 140.0 0.0 14.534 2.599 UG2 102.43 0.0026 0.0 20.534 0.053 Vel = 2.49 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 6 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn UG2 0.0 4.1 1 E 14.534 40.000 75.040 to 140.0 0.0 14.534 0.0 UG3 102.43 0.0026 0.0 54.534 0.144 Vel = 2.49 UG3 0.0 8.27 4E 113.872 500.000 75.184 to 140.0 1 G 6.326 175.552 -2.166 TEST 102.43 0.0001 1T 55.354 675.552 0.059 Vel = 0.61 100.00 Qa = 100.00 202.43 73.077 K Factor= 23.68 8 24.82 1.101 0.0 1.500 25.665 K Factor=4.90 to 150.0 0.0 0.0 -0.650 9 24.82 0.1020 0.0 1.500 0.153 Vel = 8.36 9 0.0 1.394 1 E 4.762 12.410 25.168 to 150.0 0.0 4.761 0.0 10 24.82 0.0321 0.0 17.171 0.552 Vel = 5.22 10 24.63 1.394 0.0 10.720 25.720 to 150.0 0.0 0.0 0.0 2 49.45 0.1151 0.0 10.720 1.234 Vel = 10.40 0.0 49.45 26.954 K Factor= 9.52 11 24.63 1.101 1 T 9.563 1.500 25.263 K Factor=4.90 to 150.0 0.0 9.562 -0.650 10 24.63 0.1001 0.0 11.062 1.107 Vel = 8.30 0.0 24.63 25.720 K Factor= 4.86 12 27.78 1.101 0.0 1.500 32.143 K Factor=4.90 to 150.0 0.0 0.0 -0.650 13 27.78 0.1253 0.0 1.500 0.188 Vel = 9.36 13 0.0 1.394 1 E 4.762 1.080 31.681 to 150.0 1T 9.523 14.284 0.0 3 27.78 0.0396 0.0 15.364 0.609 Vel = 5.84 0.0 27.78 32.290 K Factor= 4.89 4 49.76 2.003 1 E 6.482 10.260 42.022 to 150.0 0.0 6.482 0.0 36 49.76 0.0199 0.0 16.742 0.333 Vel = 5.07 36 0.0 2.003 0.0 7.320 42.355 to 150.0 0.0 0.0 0.0 21 49.76 0.0199 0.0 7.320 0.146 Vel = 5.07 21 0.0 2.003 3E 19.447 145.623 42.501 to 150.0 1 T 12.965 32.412 0.0 21A 49.76 0.0199 0.0 178.035 3.547 Vel = 5.07 21A 0.0 2.157 2E 12.307 10.167 46.048 to 120.0 1 B 7.384 19.691 3.000 * Fixed loss = 3 R4 49.76 0.0210 1 Fsp 0.0 29.858 0.627 Vel = 4.37 R4 0.0 4.26 1 E 13.167 23.000 49.675 to 120.0 0.0 13.167 9.961 R3 49.76 0.0008 0.0 36.167 0.028 Vel = 1.12 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 7 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn R3 0.0 4.26 1 T 26.334 0.500 59.664 to 120.0 0.0 26.334 0.0 14 49.76 0.0007 0.0 26.834 0.020 Vel = 1.12 14 -5.75 4.26 7E 92.17 250.710 59.684 to 120.0 0.0 92.170 0.0 6 44.01 0.0006 0.0 342.880 0.209 Vel = 0.99 0.0 44.01 59.893 K Factor= 5.69 14 5.74 2.003 9E 58.341 338.900 59.684 to 150.0 7T 90.753 149.094 0.0 5 5.74. 0.0004 0.0 487.994 0.179 Vel = 0.58 0.0 5.74 59.863 K Factor= 0.74 General Calculation Program Job - THE RESIDENCE AT WINDSOR FARMS Date - 10/21/13 File - C: \HES\HydraCALC\Ver50\Data\Jobs\RES CALC AREA l .wxfTime - 12 : 02 : 14 AREA CALCULATED - HEAD FLOW SUMMARY Actual Req. Delta Actual Req. Delta ID K-Factor Flow Flow Flow. Press . Press. Press 1 4 . 900 25 . 20 25.20 0 . 00 26. 449 Pt 26. 449 0.000 8 4 . 900 24 . 82 17 . 00 7 . 82 25. 665 Pt 12 . 037 13. 628 11 4 . 900 24 . 63 13. 80 10 . 83 25.263 Pt 7 . 932 17 . 331 12 4 . 900 27 . 78 25 . 30 2 . 48 32 . 143 Pt 26. 659 5. 484 Total K Factors . . . . 4 Total Fixed Flows . . . 0 Sum Actual Flow. . . . 102 . 43 Sum Required Flow. . . 81 .30 Sum Delta Flow . . . . 21 . 13 Max Delta Flow . . . . 10 .83 Max Delta Pressure . . 17 .331 AREA CALCULATED - COMPLETE SUMMARY Start Finish Diam. Start Normal Pf Elev/Fixed Flow Vel Point Point Pres . Pres . Pres . 1 <- 2 _ 1 . 101 26. 449 1 . 154 -0 . 650 25. 20 8 . 49 2 <- 3 1 . 394 26. 954 5 .336 0 . 000 74 . 65 15. 69 3 <- 4 1 . 394 32 . 290 9 .732 0 . 000 102 . 43 21 .53 4 <- 29 2 . 003 42 . 022 0 . 179 0 . 000 52 . 68 5. 36 29 <- 30 2 . 003 42 .201 0 . 159 0 . 000 52 . 68 5. 36 30 <- 31 2 . 003 42 . 360 0 . 403 0 . 000 52 . 68 5 . 36 31 <- 32 2 . 003 42 . 763 0 . 632 0 . 000 1 ` : 52 . 68 5. 36 32 <- 32A 2 . 003 43 . 394 2 . 462 0. 000 52 . 68 5. 36 32A <- R2 2 . 157 45 . 856 0 . 992 3 .000 52 . 68 4 . 62 R2 <- R1 4 .260 49. 849 0 . 031 9.961 52 . 68 1. 19 R1 <- 5 4 .260 59 . 841 0 . 023 0.000 52.. 68 1 . 19 5 <- 6 4 .260 59. 863 0. 029 0 .000 58 . 42 1 . 32 6 <- TOR 4 .260 59. 893 0 . 135 0 .000 102 . 43 2 . 31 TOR <- BOR 4 .260 60 . 027 0 . 063 6. 681 102 . 43 2 . 31 BOR <- UG1 4 .260 66. 772 0. 000 5. 616 102 . 43 2 . 31 UG1 <- UG2 4 . 100 72 . 388 0 . 054 2 .599 102 . 43 2 . 49 UG2 <- UG3 4 . 100 75. 040 0 . 143 0.000 102 . 43 2 . 49 UG3 <- TEST 8 .270 75 . 184 0. 058 -2 . 165 102 . 43 0 . 61 8 <- 9 1 . 101 25. 665 0 . 152 -0. 650 24 . 82 8 . 37 9 <- 10 1 . 394 25. 168 0 . 552 0 .000 24 . 82 5.22 10 <- 2 1 . 394 25. 720 1 .234 0.000 49 . 45 10 . 40 11 <- 10 1 . 101 25.263 1. 106 -0 . 650 24 . 63 8 . 30 12 <- 13 1 . 101 32 . 143 0 . 187 -0. 650 27 . 78 9. 36 13 <- 3 1 . 394 31 . 681 0 . 608 0.000 27 . 78 5. 84 4 <- 36 2 . 003 42 . 022 0 . 334 0. 000 49 . 76 5. 07 36 <- 21 2 . 003 42 . 355 0 . 146 0. 000 49 . 76 5. 07 21 <- 21A 2 . 003 42 . 501 3. 547 0. 000 -49 . 76 5 . 07 21A <- R4 2 . 157 46. 048 0 . 627 3. 000 49 . 76 4 . 37 R4 <- R3 4 .260 49. 675 0 . 028 9. 961 49. 76 1 . 12 R3 <- 14 4 .260 59. 664 0 . 020 0. 000 49 .76 1 . 12 14 <- 6 4 . 260 59. 684 0 .209 0 .000 44 . 01 0 . 99 14 <- 5 2 . 003 59. 684 0 . 179 0 .000 5. 74 0. 58 2 r Pipe with highest velocity: 3 - 4 (21". 533) Water Supply Summary @ Point TEST Total Flow From Water Supply Curve . . . . . . . . 202 . 433 Pressure From Water Supply Curve . . . . . . . . . 89.753 System Pressure Demand At Supply Curve . . . . . . 73. 077 Safety Margin at Supply Curve. . . . . . . . . 16. 676 3 1 . . . Fire Protection by Computer Design Z . C.No.0001 [OF 9y ALLSTATE FIRE SYSTEMS 110 MURPHY RD HARTFORD, CT. 06114 860-246-7711 Job Name THE RESIDENCE AT WINDSOR FARMS Building FRONT CANOPY Location 200 DEMING STREET SOUTH WINDSOR, CT. System 4 Contract Data File RES CALC AREA 4.wxF ALLSTATE FIRE SYSTEMS Page 1 THE RESIDENCE AT WINDSOR FARMS Date Hydraulic Design Information Sheet Name - THE RESIDENCE AT DEMING Date - 10/15/13 Location - 200 DEMING STREET SOUTH WINDSOR, CT. Building - FRONT CANOPY System No. - 4 Contractor - ALLSTATE FIRE SYSTEMS Contract No. - Calculated By - PAUL FORAUER Drawing No. - FP-1 Construction: (X) Combustible ( ) Non-Combustible Ceiling Height - 810 Occupancy - LIGHT HAZARD S (X) NFPA 13 (X) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure . Curve S Other T Specific Ruling Made By Date E M Area of Sprinkler Operation - 1294 System Type Sprinkler/Nozzle Density - .10 ( ) Wet Make TYCO D Area Per Sprinkler - 120 (X) Dry Model TY-FRB E Elevation at Highest Outlet - 17. 63 ( ) Deluge Size 1/2" S Hose Allowance - Inside - ( ) Preaction K-Factor 5.6 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.155 G Hose Allowance - Outside - 100 N Note Calculation Flow Required - 308.816 Press Required - 75.475 Summary C-Factor Used: 150 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - 06/06/13 - T Time of Test - Rated Cap.- Elev.- E Static Press - 90 @ Press - R Residual Press - 70 Elev. - Well Flow - 2176 Proof Flow S Elevation - 0 U P Location - 200 DEMING STREET P L Source of Information - CONTRACT DRAWING FP0.00 Y C Commodity Class Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled % Palletized % Rack M ( ) Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Enca P• 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 G E Horizontal Barriers Provided: ater Supply Curve (C) LLSTATE FIRE SYSTEMS Page 2 HE RESIDENCE AT WINDSOR FARMS Date City Water Supply: Demand: C1 -Static Pressure : 90 D1 - Elevation 7.636 C2 -Residual Pressure: 70 D2 -System Flow 208.816 C2 - Residual Flow 2176 _ D2-System Pressure 75.475 Hose( Demand ) 100 D3 -System Demand 308.816 Safety Margin 13.985 150 140 130 P 120 R 110 E 100 C1 S 90 S 80 C2 U 70 R 60 E 50 40 30 20 10 D1 300 600 900 1200 1500 1800 2100 2400 2700 FLOW( N 11 1.85 ) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 icings Used Summary LLSTATE FIRE SYSTEMS Page 3 HE RESIDENCE AT WINDSOR FARMS Date itting Legend bbrev. Name % 9/ 1 1 Y< 1'/2 2 2% 3 3'/2 4 5 6 8 10 12 14 16 18 20 24 NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 , 0 0 ge Dry Gem DPV-1 2.2 4.9 8.9 22 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 NFPA 13 45'Elbow 1 1 1 1 2 2 3 3 3 4 5 7 9 11 13 17 .19 21 24 28 sp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow 5 NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 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 _ib Wilkins 350A Fitting generates a Fixed Loss Based on Flow Jnits Summary )iameter Units Inches .ength Units Feet -'low Units US Gallons per Minute 'ressure Units Pounds per Square Inch Jote: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. :quivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors �f 120 except as noted with *. The fittings marked with a*show equivalent lengths values upplied by manufacturers based on specific pipe diameters and CFactors and they require no djustment. All values for fittings not marked with a *will be adjusted in the calculation )r 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 ALLSTATE FIRE SYSTEMS Page 4 THE RESIDENCE AT WINDSOR FARMS Date Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Reg. 84 17.63 5.6 7.0 na 14.82 0.1 100 7.0 85 16.63 7.51 na 86 . 14.26 9.41 na 87 12.63 10.96 na 88 12.63 13.31 na 89 12.61 13.62 na 90 12.6 14.12 na 91 12.58 15.41 na 92 12.55 17.15 na 93 12.53 19.42 na 94 12.51 21.61 na 94A 12.51 23.35 na TDV 9.5 50.18 na BDV 3.0 56.07 na R6 3.0 56.3 na R5 9.5 56.06 na 95 9.5 61.85 na 6 9.5 63.35 na TOR 9.5 63.85 na BOR 1.0 70.77 na UG1 1.0 74.09 na UG2 -5.0 76.89 na UG3 -5.0 77.42 na TEST 0.0 75.48 na 100.0 96 16.13 5.6 7.19 na 15.01 0.1 100 7.0 97 15.37 7.58 na 98 16.13 5.6 7.91 na 15.75 0.1 100 7.0 99 15.37 8.31 na 100 12.63 11.9 na 101 15.15 5.6 8.49 na 16.32 0.1 100 TO 102 16.13 5.6 9.11 na 16.9 0.1 100 7.0 103 15.37 9.52 na 104 13.61 5.6 12.07 na 19.46 0.1 75 7.0 105 12.61 12.63 na 106 13.6 5.6 12.54 na 19.83 0.1 120 7.0 107 12.6 13.1 na 108 13.58 5.6 13.72 na 20.74 0.1 120 7.0 109 12.58 14.3 na 110 13.55 5.6 15.32 na 21.92 0.1 120 7.0 111 12.55 15.91 na 112 13.53 5.6 17.42 na 23.37 0.1 120 7.0 113 12.53 18.03 na 114 13.51 5.6 19.44 na 24.69 0.1 75 7.0 115 12.51 20.07 na 14 9.5 61.87 na 52 10.0 62.8 na 64 10.0 62.84 na 65 10.0 62.88 na 5 9.5 63.34 na The maximum velocity is 19.97 and it occurs in the pipe between nodes 94 and 94A I✓inal Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 5 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 84 14.82 1.049 0.0 1.000 7.000 K Factor=5.60 to 120.0 0.0 0.0 0.433 85 14.82 0.0750 0.0 1.000 0.075 Vel = 5.50 85 0.0 1.049 2E 4.0 7.690 7.508 to 120.0 0.0 4.000 1.026 86 14.82 0.0748 0.0 11.690 0.874 Vel = 5.50 86 16.31 1.38 IT 6.0 4.960 9.408 to 120.0 0.0 6.000 0.706 87 31.13 0.0776 0.0 10.960 0.850 Vel = 6.68 87 15.02 1.38 IF 1.0 7.580 10.964 to 120.0 IT 6.0 7.000 0.0 88 46.15 0.1608 0.0 14.580 2.344 Vel = 9.90 88 32.65 2.067 0.0 5.010 13.308 to 120.0 0.0 0.0 0.009 89 78.8 0.0603 0.0 5.010 0.302 Vel = 7.53 89 19.46 2.067 0.0 5.500 13.619 to 120.0 0.0 0.0 0.004 90 98.26 0.0911 0.0 5.500 0.501 Vel = 9.39 90 19.82 2.067 0.0 10.000 14.124 to 120.0 0.0 0.0 0.009 91 118.08 0.1277 0.0 10.000 1.277 Vel = 11.29 91 20.75 2.067 0.0 10.000 15.410 to 120.0 0.0 0.0 0.013 92 138.83 0.1724 0.0 10.000 1.724 Vel = 13.27 92 21.92 2.067 0.0 10.000 17.147 to 120.0 0.0 0.0 0.009 - 93 160.75 0.2261 0.0 10.000 2.261 Vel = 15.37 93 23.37 2.067 0.0 7.500 19.417 to 120.0 0.0 0.0 0.009 94 184.12 0.2907 0.0 7.500 2.180 Vel = 17.60 94 24.70 2.067 0.0 4.750 21.606 to 120.0 0.0 0.0 0.0 94A 208.82 0.3667 0'.0 4.750 1.742 Vel = 19.97 94A 0.0 2.157 5E 30.767 54.860 23.348 to 120.0 0.0 30.767 1.304 TDV 208.82 0.2981 0.0 85.627 25.526 Vel = 18.33 TDV 0.0 2.635 1 E 8.237 6.500 50.178 to 120.0 1 B 9.61 20.867 2.815 BDV 208.82 0.1124 1 Dge 3.02 27.367 3.077 Vel = 12.29 BDV 0.0 2.635 0.0 2.000 56.070 to 120.0 0.0 0.0 0.0 R6 208.82 0.1125 0.0 2.000 0.225 Vel = 12.29 R6 0.0 2.635 2E 16.474 6.500 56.295 to 120.0 0.0 16.474 -2.815 R5 208.82 0.1125 0.0 22.974 2.584 Vel = 12.29 R5 0.0 2.635 1 E 8.237 26.780 56.064 to 120.0 1 T 16.474 24.711 0.0 95 208.82 0.1125 0.0 51.491 5.791 Vel = 12.29 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 6 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 95 -16.21 4.26 3E 39.501 120.260 61.855 to 120.0 0.0 39.501 0.0 6 192.61 0.0093 0.0 159.761 1.491 Vel = 4.34 6 16.21 4.26 1 E 13.167 33.260 63.346 to 120.0 0.0 13.167 0.0 TOR 208.82 0.0109 0.0 46.427 0.504 Vel = 4.70 TOR 0.0 4.26 1 E 13.167 8.500 63.850 to 120.0 1 Fsp 0.0 13.167 6.681 * Fixed loss = 3 BOR 208.82 0.0108 0.0 21.667 0.235 Vel = 4.70 BOR 0.0 4.26 1Zib 0.0 0.010 70.766 to 120.0 0.0 0.0 3.321 * Fixed loss = 3.321 UG1 208.82 0.0 0.0 0.010 0.0 Vel = 4.70 UG1 0.0 4.1 1 E 14.534 6.000 74.087 to 140.0 0.0 14.534 2.599 UG2 208.82 0.0098 0.0 20.534 0.202 Vel = 5.07 UG2 0.0 4.1 1 E 14.534 40.000 76.888 to 140.0 0.0 14.534 0.0 UG3 208.82 0.0098 0.0 54.534 0.535 Vel = 5.07 UG3 0.0 8.27 4E 113.872 500.000 77.423 to 140.0 1 G 6.326 175.552 -2.166 TEST 208.82 0.0003 IT 55.354 675.552 0.218 Vel = 1.25 100.00 Qa = 100.00 308.82 75.475 K Factor= 35.55 96 15.01 1.049 0.0 0.870 7.185 K Factor= 5.60 to 120.0 0.0 0.0 0.329 97 15.01 0.0770 0.0 0.870 0.067 Vel = 5.57 97 0.0 1.049 2E 4.0 22.700 7.581 to 120.0 2F 2.0 6.000 1.187 87 15.01 0.0765 0.0 28.700 2.196 Vel = 5.57 0.0 15.01 10.964 K Factor= 4.53 98 15.75 1.049 0.0 0.870 7.912 K Factor= 5.60 to 120.0 0.0 0.0 0.329 99 15.75 0.0839 0.0 0.87.0 0.073 Vel = 5.85 99 0.0 1.049 2E 4.0 22.700 8.314 to. 120.0 2F 2.0 6.000 1.187 100 15.75 0.0837 0.0 28.700 2.401 Vel = 5.85 100 16.90 1.38 1 F 1.0 9.580 11.902 to 120.0 1T 6.0 7.000 0.0 88 32.65 0.0848 0.0 16.580 1.406 Vel = 7.00 0.0 32.65 13.308 K Factor= 8.95 101 16.32 1.049 1 T 5.0 0.940 8.492 K Factor= 5.60 to 120.0 0.0 5.000 0.385 86 16.32 0.0894 0.0 5.940 0.531 Vel = 6.06 0.0 16.32 9.408 K Factor= 5.32 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 7 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 102 16.90 1.049 0.0 0.870 9.108 _ K Factor= 5.60 to 120.0 0.0 0.0 0.329 103 16.9 0.0954 0.0 0.870 0.083 Vel = 6.27 103 0.0 1.049 1 E 2.0 5.540 9.520 to 120.0 1 T 5.0 7.000 1.187 100 16.9 0.0953 0.0 12.540 1.195 Vel = 6.27 0.0 16.90 11.902 K Factor= 4.90 104 19.46 1.049 0.0 1.000 12.073 K Factor= 5.60 to 120.0 0.0 0.0 0.433 105 - 19.46 0.1240 0.0 1.000 0.124 Vel = 7.22 105 0.0 1.049 1 E 2.0 1.000 12.630 to 120.0 IT 5.0 7.000 0.0 89 19.46 0.1236 0.0 8.000 0.989 Vel = 7.22 0.0 19.46 13.619 K Factor= 5.27 106 19.83 1.049 0.0 1.000 12.537 K Factor= 5.60 to 120.0 0.0 0.0 0.433 107 19.83 01280 0.0 1.000 0.128 Vel = 7.36 107 0.0 1.049 1 E 2.0 1.010 13.098 to 120.0 1 T 5.0 7.000 0.0 90 19.83 0.1281 0.0 8.010 1.026 Vel = 7.36 0.0 19.83 14.124 K Factor= 5.28 108 20.74 1.049 0.0 1.000 13.723 K Factor= 5.60 to 120.0 0.0 0.0 0.433 109 20.74 0.1390 0.0 1.000 0.139 Vel = 7.70 109 0.0 1.049 1 E 2.0 1.010 14.295 to 120.0 IT 5.0 7.000 0.0 91 20.74 0.1392 0.0 8.010 1.115 Vel = 7.70 0.0 20.74 15.410 K Factor= 5.28 110 21.92 1.049 0.0 1.000 15.325 K Factor= 5.60 to 120.0 0.0 0.0 0.433 111 21.92 0.1540 0.0 1.000 0.154 Vel = 8.14 111 0.0 1.049 1E 2.0 1.010 15.912 to 120.0 IT 5.0 7.000 0.0 92 21.92 0.1542 0.0 8.010 1.235 Vel = 8.14 0.0 21.92 17.147 K Factor= 5.29 112 23.37 1.049 0.0 1.000 17.420 K Factor= 5.60 to 120.0 0.0 0.0 0.433 113 23.37 0.1730 0.0 1.000 0.173 Vel = 8.68 113 0.0 1.049 1 E 2.0 1.010 18.026 to 120.0 1 T 5.0 7.000 0.0 . 93 23.37 0.1737 0.0 8.010 1.391 Vel = 8.68 0.0 23.37 19.417 K Factor= 5.30 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 8 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 114 24.69 1.049 0.0 1.000 19.441 K Factor= 5.60 to 120.0 0.0 0.0 0.433 115 24.69 0.1920 0.0 1.000 0.192 Vel = 9.17 115 0.0 1.049 1 E 2.0 1.010 20.066 to 120.0 1 T 5.0 7.000 0.0 94 24.69 0.1923 0.0 8.010 1.540 Vel = 9.17 0.0 24.69 21.606 K Factor= 5.31 95 16.20 4.26 4E 52.668 130.450 61.855 to 120.0 0.0 52.668 0.0 14 16.2 0.0001 0.0 183.118 0.017 Vel = 0.36 14 0.0 2.067 6E 30.0 271.990 61.872 to 120.0 5T 50.0 80.000 -0.217 52 16.2 0.0032 0.0 351.990 1.142 Vel = 1.55 52 0.0 2.067 0.0 14.350 62.797 to 120.0 0.0 0.0 0.0 64 16.2 0.0032 0.0 14.350 0.046 Vel = 1.55 64 0.0 2.067 0.0 12.000 62.843 to 120.0 0.0 0.0 0.0 65 16.2 0.0032 0.0 12.000 0.039 Vel = 1.55 65 0.0 2.067 2T 20.0 40.560 62.882 to 120.0 3E 15.0 35.000 0.217 5 16.2 0.0032 0.0 75.560 0.245 Vel = 1.55 5 0.0 4.26 1 T 26.334 2.360 63.344 to 120.0 0.0 26.334 0.0 6 16.2 0.0001 0.0 28.694 0.002 Vel = 0.36 0.0 16.20 63.346 K Factor= 2.04 General Calculation Program Job - THE RESIDENCE AT WINDSOR FARMS Date 10/21/13 File - C: \HES\HydraCALC\Ver50\Data\Jobs\RES CALC AREA 4 .wxfTime - 12 : 09: 54 AREA CALCULATED - HEAD. FLOW SUMMARY Actual Req. Delta Actual Req. Delta ID K-Factor Flow Flow Flow. Press . Press. Press 84 5. 600 14 . 82 14 . 82 0 . 00 7 . 000 Pt 7 . 000 0 . 000 96 5. 600 15. 01 14 . 82 0 . 19 7 . 185 Pt 7 . 000 0 . 185 98 5. 600 15. 75 14 . 82 0 . 94 7 . 912 Pt 7 . 000 0 . 912 101 5. 600 16. 32 14 . 82 1 . 50 8 . 492 Pt 7 . 000 1 . 492 102 5. 600 16. 90 14 . 82 2 . 08 . 9 . 108 Pt 7 . 000 2 . 108 104 5. 600 19 . 46 14 . 82 4 . 64 12 . 073 Pt 7 . 000 5 . 073 106 5. 600 19. 83 14 . 82 5. 01 12 . 537 Pt 7 . 000 5. 537 108 5. 600 20 . 74 14 . 82 5. 93 13.723 Pt 7 . 000 6. 723 110 5. 600 21 . 92 14 . 82 7 . 11 15. 325 Pt 7 . 000 8 . 325 112 5. 600 23 . 37 14 . 82 8 . 56 17 . 420 Pt 7 . 000 10 . 420 114 5. 600 24 . 69 14 . 82 9 . 88 19. 441 Pt 7 . 000 12 . 441 Total K Factors . . . . 11 Total Fixed Flows . . . 0 Sum Actual Flow. . . 208 . 82 Sum Required Flow. . . 162 . 98 Sum Delta Flow . . . 45 . 84 Max Delta Flow . . . . 9 . 88 Max Delta Pressure . . 12 . 441 AREA CALCULATED - COMPLETE SUMMARY Start Finish Diam. Start Normal Pf Elev/Fixed Flow Vel Point Point Pres. Pres . 1 Pres . 84 < 85 1 . 049 7. 000 0 . 075 0. 433 14 . 82 5.50 85 <- 86 1 . 049 7 .508 0. 873 1 . 026 14 . 82 5 . 50 86 <- 87 1 . 380 9. 408 0. 851 0 . 706 31 . 13 6. 68 . 87 <- 88 1 . 380 10. 964 2 .343 0 . 000 46. 15 9 . 90 88 <- 89 2 . 067 13.308 0 . 303 0. 009 78 . 80 7 . 53 89 <- 90 2 . 067 13. 619 0 . 500 0. 004 98 .26 9 . 39 90 <- 91 2 . 067 14 . 124 1 .278 0 . 009 118 . 08 11 .29 91 <- 92 2 . 067 15. 410 1 . 724 0 . 013 138. 83 13 .27 92 <- 93 2 . 067 17 . 147 2 . 261 0. 009 160 . 75 15. 37 93 <- 94 2 . 067 19 . 417 2 . 180 0. 009 184 . 12 17 . 60 94 <- 94A 2 . 067 21 . 606 1. 743 0. 000 208 . 82 19. 97 94A <- TDV 2 . 157 23. 348 25.526 1 . 304 208 . 82 18 . 33 TDV <- BDV 2 . 635 50 . 178 3. 078 2 . 815 208 . 82 12 .29 BDV <- R6 2 . 635 56. 071 0 .225 0 . 000 268 . 82 12 .29 R6 <- R5 2 . 635 56.295 2 . 584 -2 . 815 208 . 82 12 .29 R5 <- 95 2 . 635 56.064 5.791 0 .000 208 . 82 12 . 29 95 <- 6 4 .260 61 . 855 1 . 491 0. 000 192 . 61 4 . 34 6 <- TOR 4 .260 63 . 346 0 .503 0 . 000 208 . 82 4 . 70 TOR <- BOR 4 .260 63 . 849 0 . 235 6. 681 208 . 82 4 . 70 BOR <- UG1 4 .260 70 . 766 0 . 000 3 . 321 208 . 82 4 . 70 UG1 <- UG2 4 . 100 74 . 087 0 .202 2 .599 208 . 82 5. 07 UG2 <- UG3 4 . 100 76. 887 0 .536 0 . 000 208 . 82 5. 07 UG3 <- TEST 8 .270 77 . 423 0 .218 -2 . 165 208 . 82 1 .25 96 <- 97 1 . 049 7 . 185 0 . 067 0.329 15. 01 5 . 57 97 <- 87 1 . 049 7 .581 2 . 196 1. 187 15. 01 5 . 57 98 <- 99 1 . 049 7 . 912 0 . 073 0. 329 2 i 15. 75 5 . 85 99 <- 100 1. 049 8 . 314 2 . 401 1 . 187 15.75 5. 85 100 <- 88 1 . 380 11 . 902 1 . 405 0 . 000 32 . 65 7 . 00 101 <- 86 1. 049 8 . 492 0 . 531 0 . 385 16. 32 6. 06 102 <- 103 1 . 049 9. 108 0 . 083 0 . 329 16..90 6.27 103 <- 100 1. 049 9. 520 1 . 195 1 . 187 16. 90 6.27 104 <- 105 1. 049 12 . 073 0 . 124 0 . 433 19. 46 7 .22 105 <- 89 1 . 049 12 . 630 0 . 989 0 . 000 19. 46 7 .22 106 <- 107 1 . 049 12 . 537 0 . 128 0 . 433 19 . 83 7 . 36 107 <- 90 1 . 049 13 . 098 1 . 026 0 . 000 19. 83 7 . 36 108 <- 109 1. 049 13. 723 0 . 139 0 . 433 20 . 74 7 . 70 109 <- 91 1 . 049 14 .295 1 . 115 0 . 000 20 . 74 7 . 70 110 <- 111 1 . 049 15. 325 0 . 154 0 . 433 21 . 92 8 . 14 1.11 <- 92 1 . 049 15. 912 1 .235 0 . 000 21 . 92 8 . 14 112 <- 113 1 . 049 17 . 420 0 . 174 0 . 433 23 . 37 8 . 68 113 <- 93 1 . 049 18 . 026 1 . 391 0 . 000 23. 37 8 . 68 114 <- 115 1. 049 19. 441 0 . 192 0 . 433 24 . 69 9. 17 115 <- 94 1. 049 20 . 066 1 . 539 0 . 000 24 . 69 9 . 17 95 <- 14 4 .260 61,. 855 0 . 018 0 . 000 16.20 0 . 36 14 <- 52 2 . 067 61 . 872 1 . 141 -0 .217 16.20 1 . 55 52 <- 64 2 . 067 62 . 797 0 . 047 0 . 000 16.20 1 . 55 64 <- 65 2 . 067 62 . 843 0 . 039 0 . 000 16.20 1 . 55 65 <- 5 2. 067 62 . 882 0 .245 0 .217 16.20 1 . 55 5 <- 6 4 .260 63. 343 0 . 003 0 . 000 16.20 0 . 36 Pipe with highest velocity: 94 - 94A (19. 965) Water Supply Summary @ Point TEST 3 Total Flow From Water Supply Curve . . . . . . . . 308 . 816 Pressure From Water Supply Curve . . . . . . . . . 89 . 460 System Pressure Demand At Supply Curve . . . . . . 75. 475 Safety Margin at Supply Curve. . . . . . . . 13. 985 4 <9 0 _ _ _ Fire Protection by Computer Design Lf M0.Gab � i 0 ALLSTATE FIRE SYSTEMS �r 110 MURPHY RD HARTFORD, CT. 06114 860-246-7711 Job Name THE RESIDENCE AT WINDSOR FARMS Building 3RD FLOOR ELEV. LOBBY Location 200 DEMING STREET SOUTH WINDSOR, CT. System 2 Contract Data File RES CALC AREA 2.wxf ALLSTATE FIRE SYSTEMS Page 1 THE RESIDENCE AT WINDSOR FARMS Date Hydraulic Design Information Sheet Name - THE RESIDENCE AT WINDSOR FARMS Date - 10/15/13 Location - 200 DEMING STREET SOUTH WINDSOR, CT. Building - 3RD FLOOR ELEV. LOBBY System No. - 2 Contractor - ALLSTATE FIRE SYSTEMS Contract No. - Calculated By - PAUL FORAUER Drawing No. - FP-3 Construction: ( ) Combustible (X) Non-Combustible Ceiling Height - 810 Occupancy - LIGHT HAZARD S (X) NFPA 13 (X) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ). Ex.Haz. Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure Curve S Other T Specific Ruling Made By Date E M Area of Sprinkler Operation - 1012 System Type Sprinkler/Nozzle Density - .10 (X) Wet Make TYCO D Area Per Sprinkler - 252 ( ) Dry Model RFII E Elevation at Highest Outlet - 31 ( ) Deluge Size 1/2" S Hose Allowance - Inside - ( ) Preaction K-Factor 5. 6 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.155 G Hose Allowance - Outside - 100 N Note Calculation Flow Required - 294 .363 Press Required - 50.388 Summary C-Factor Used: 150 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or .Reservoir: A Date of Test - 06/06/13 Cap. - T Time of Test - Rated Cap.- Elev.- E Static Press - 90 @ Press - R Residual Press - 70 Elev. - Well Flow - 2176 Proof Flow S Elevation - 0 U P Location - 200 DEMING STREET P L Source of Information - CONTRACT DRAWING FP0.00 Y C Commodity Class Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled % 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 0 C R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse G E Horizontal Barriers Provided: ater Supply Curve (C) LLSTATE FIRE SYSTEMS Page 2 HE RESIDENCE AT WINDSOR FARMS Date City Water Supply: Demand: C1 -Static Pressure : 90 D1 - Elevation 13.426 C2 - Residual Pressure: 70 D2-System Flow 19 .4 63 C2 - Residual Flow 2176 D2-System Pressure 50.388 Hose ( Demand ) 100 D3-System Demand 294.363 Safety Margin 39.118 150 140 130 P 120 R 110 E 100 C1 S 90 S 80 U 70 C2 R 60 D2 E 50 40 30 20 10 300 600 900 1200 1500 1800 2100 2400 2700 FLOW( NA1.85 ) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 ittings Used Summary LLSTATE FIRE SYSTEMS Page 3 HE RESIDENCE AT WINDSOR FARMS Date itting Legend bbrev. Name '/2 3/4 1 1 Y4 1'/2 2 2'/2 3 3'/2 4 5 6 8 10 12 14 16 18 20 24 NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 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 sp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 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 ib Wilkins 350A Fitting generates a Fixed Loss Based on Flow Jnits Summary Nameter Units Inches .ength Units Feet 'low Units US Gallons per Minute 'ressure Units Pounds per Square Inch Jote: 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 �f 120 except as noted with *. The fittings marked with a*show equivalent lengths values ,upplied 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 Dr 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 ALLSTATE FIRE SYSTEMS Page 4 THE RESIDENCE AT WINDSOR FARMS Date Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Reg. 15 31.0 5.6 7.0 na 14.82 0.1 101 7.0 16 32.5 6.41 na 17 32.5 7.28 na 18 32.5 7.72 na 19 32.5 9.66 na 20 32.5 9.94 na 21 32.5 11.56 na 21A 32.5 22.77 na R4 32.5 27.75 na R3 9.5 37.8 na 14 9.5 37.87 na 6 9.5 38.53 na TOR 9.5 38.97 na BOR 1.0 45.85 na UG1 1.0 49.12 na UG2 -5.0 51.89 na UG3 -5.0 52.36 na TEST 0.0 50.39 na 100.0 22 31.0 5.6 7.28 na 15.11 0.1 76 7.0 23 32.5 6.69 na 24 31.0 5.6 7.68 na 15.52 0.1 56 7.0 25 32.5 7.1 na 26 31.0 5.6 9.99 na 17.7 0.1 148 7.0 27 31.0 5.6 10.58 na 18.21 0.1 159 7.0 28 32.5 10.01 na 4 32.5 11.51 na 29 32.5 11.56 na 30 32.5 11.67 na 31 32.5 12.22 na 32 32.5 13.63 na 32A 32.5 21.94 na R2 32.5 28.28 na R1 9.5 '38.35 na 5 9.5 38.43 na 33 31.0 5.6 10.8 na 18.4 0.1 65 7.0 34 32.5 10.24 na 35 32.5 10.68 na 36 32.5 11.5 na 37 31.0 5.6 10.69 na 18.31 0.1 93 7.0 38 31.0 5.6 10.73 na 18.35 0.1 121 7.0 39 32.5 10.17 na 40 31.0 5.6 11.11 na 18.67 0.1 41 7.0 41 32.5 10.55 na 42 31.0 5.6 11.21 na 18.75 0.1 122 7.0 43 32.5 10.65 na 44 31.0 5.6 13.44 na 20.53 0.1 118 7.0 45 32.5 12.9 na The maximum velocity is 10.35 and it occurs in the pipe between nodes 32 and 32A Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 5 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 15 14.82 1.101 0.0 1.500 7.000 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 16 14.82 0.0393 0.0 1.500 0.059 Vel = 4.99 16 0.0 1.101 2E 7.65 14.540 6.409 to 150.0 0.0 7.650 0.0 17 14.82 0.0391 0.0 22.190 0.867 Vel = 4.99 17 15.10 1.394 0.0 9.670 7.276 to 150.0 0.0 0.0 0.0 18 29.92 0.0454 0.0 9.670 0.439 Vel = 6.29 18 15.52 1.394 1 E 4.762 5.470 7.715 to 150.0 IT 9.523 14.284 0.0 19 45.44 0.0985 0.0 19.754 1.945 Vel = 9.55 19 0.0 1.598 0.0 5.530 9.660 to 150.0 0.0 0.0 0.0 20 45.44 0.0505 0.0 5.530 0.279 Vel = 7.27 20 17.70 1.598 IT 11.656 5.730 9.939 to 150.0 0.0 11.656 0.0 21 63.14 0.0931 0.0 17.386 1.618 Vel = 10.10 21 29.56 2.003 3E 19.447 145.623 11.557 to 150.0 IT 12.965 32.412 0.0 21 A 92.7 0.0630 0.0 178.035 11.214 Vel = 9.44 21 A 0.0 2.157 2 E 12.307 10.167 22.771 to 120.0 1 B 7.384 19.691 3.000 * Fixed loss = 3 R4 92.7 0.0663 1 Fsp 0.0 29.858 1.981 Vel = 8.14 R4 0.0 4.26 1 E 13.167 23.000 27.752 to 120.0 0.0 13.167 9.961 R3 92.7 0.0024 0.0 36.167 0.087 Vel = 2.09 R3 0.0 4.26 1 T 26.334 0.500 37.800 to 120.0 0.0 26.334 0.0 14 92.7 0.0024 0.0 26.834 0.065 Vel = 2.09 14 -10.65 4.26 7E 92.17 250.710 37.865 to 120.0 0.0 92.170 0.0 6 82.05 ' 0.0019 0.0 342.880 0.660 Vel = 1.85 6 112.31 4.26 1 E 13.167 33.260 38.525 to 120.0 0.0 13.167 0.0 TOR 194.36 0.0095 0.0 46.427 0.441 Vel = 4.37 TOR 0.0 4.26 1 E 13.167 8.500 38.966 to 120.0 1 Fsp 0.0 13.167 6.681 * Fixed loss = 3 BOR 194.36 0.0095 0.0 21.667 0.206 Vel = 4.37 BOR 0.0 4.26 1Zib 0.0 0.010 45.853 to 120.0 0.0 0.0 3.266 * Fixed loss = 3.266 UG1 194.36 0.0 0.0 0.010 0.0 Vel = 4.37 UG1 0.0 4.1 1 E 14.534 6.000 49.119 to 140.0 0.0 14.534 2.599 UG2 194.36 0.0086 0.0 20.534 0.176 Vel = 4.72 UG2 0.0 4.1 1 E 14.534 40.000 51.894 to 140.0 0.0 14.534 0.0 UG3 194.36 0.0086 0.0 54.534 0.469 Vel = 4.72 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 6 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv **** ** Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn UG3 0.0 8.27 4E 113.872 500.000 52.363 to 140.0 1 G 6.326 175.552 -2.166 TEST 194.36 0.0003 1T 55.354 675.552 0.191 Vel= 1.16 100.00 Qa = 100.00 294.36 50.388 K Factor= 41.47 22 15.11 1.101 0.0 1.500 7.277 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 23 15.11 0.0407 . 0.0 1.500 0.061 Vel = 5.09 23 0.0 1.101 1 E 3.825 1.130 6.688 to 150.0 1 T 9.563 13.387 0.0 17 15.11 0.0405 0.0 14.517 0.588 Vel = `5.09 0.0 15.11 7.276 K Factor= 5.60 24 15.52 1.101 0.0 1.500 7.683 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 25 15.52 0.0427 0.0 1.500 0.064 Vel = 5.23 25 0.0 1.101 1 E 3.825 1.130 7.097 to 150.0 1 T 9.563 13.387 0.0 18 15.52 0.0426 0.0 14.517 0.618 Vel = 5.23 0.0 15.52 7.715 K Factor= 5.59 26 17.70 1.101 1 T 9.563 1.500 9.989 K Factor= 5.60 to 150.0 0.0 9.562 -0.650 20 17.7 0.0542 0.0 11.062 0.600 Vel= 5.96 0.0 17.70 9.939 K Factor= 5.61 27 18.21 1.101 0.0 1.500 10.578 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 28 18.21 0.0573 0.0 1.500 0.086 Vel = 6.14 28 0.0 1.101 1 E 3.825 3.200 10.014 to 150.0 2T 19.125 22.951 0.0 4 18.21 0.0572 0.0 26.151 1.496 Vel = 6.14 4 7.16 2.003 0.0 8.080 11.510 to 150.0 0.0 0.0 0.0 29 25.37 0.0057 0.0 8.080 0.046 Vel = 2.58 29 18.67 2.003 0.0 7.190 11.556 to 150.0 0.0 0.0 0.0 30 44.04 0.0160 0.0 7.190 0.115 Vel = 4.48 30 18.34 2.003 0.0 18.190 11.671 to 150.0 0.0 0.0 0.0 31 62.38 0.0303 0.0 18.190 0.551 Vel = 6.35 31 18.76 2.003 1 E 6.482 9.090 12.222 to 150.0 1 T 12.965 19.447 0.0 32 81.14 0.0492 0.0 28.537 1.404 Vel = 8.26 32 20.53 2.003 1 E 6.482 91.758 13.626 to 150.0 1 T 12.965 19.447 0.0 32A 101.67 0.0747 0.0 111.205 8.310 Vel = 10.35 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 7 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 32A 0.0 2.157 2E 12.307 10.542 21.936 to 120.0 1T 12.307 31.998 3.000 *Fixed loss = 3 R2 101.67 0.0787 1 B 7.384 42.540 3.349 Vel = 8.93 1 Fsp 0.0 R2 0.0 4.26 1 E 13.167 23.000 28.285 to 120.0 0.0 13.167 9.961 R1 101.67 0.0029 0.0 36.167 0.104 Vel = 2.29 R1 0.0 4.26 1T 26.334 0.500 38.350 to 120.0 0.0 26.334 0.0 5 101.67 0.0028 0.0 26.834 0.076 Vel = 2.29 5 10.65 4.26 IT 26.334 2.360 38.426 to 120.0 0.0 26.334 0.0 6 112.32 0.0035 0.0 28.694 0.099 Vel = 2.53 0.0 112.32 38.525 K Factor= 18.10 33 18.40 1.101 0.0 1.500 10.797 K Factor=5.60 to 150.0 0.0 0.0 -0.650 34 18.4 0.0587 0.0 1.500 0.088 Vel = 6.20 34 0.0 1.101 1 E 3.825 3.820 10.235 to 150.0 0.0 3.825 0.0 35 18.4 0.0583 0.0 7.645 0.446 Vel = 6.20 35 18.31 1.394 IT 9.523 2.840 10.681 to 150.0 0.0 9.523 0.0 36 36.71 0.0663 0.0 12.363 0.820 Vel = 7.72 36 -7.16 2.003 0.0 7.320 11.501 to 150.0 0.0 0.0 0.0 21 29.55 0.0077 0.0 7.320 0.056 Vel = 3.01 0.0 29.55 11.557 K Factor= 8.69 37 18.31 1.101 1 T 9.563 1.500 10.691 K Factor= 5.60 to 150.0 0.0 9.562 -0.650 35 18.31 0.0579 0.0 11.062 0.640 Vel = 6.17 0.0 18.31 10.681 K Factor= 5.60 36 7.16 2.003 1 E 6.482 10.260 11.501 to 150.0 0.0 6.482 0.0 4 7.16 0.0005 0.0 16.742 0.009 Vel = 0.73 0.0 7.16 11.510 K Factor= 2.11 38 18.35 1.101 0.0 1.500 10.732 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 39 18.35 0.0587 0.0 1.500 0.088 Vel = 6.18 39 0.0 1.101 1 E 3.825 2.930 10.170 to 150.0 2T 19.125 22.951 0.0 30 18.35 0.0580 0.0 25.881 1.501 Vel = 6.18 0.0 18.35 11.671 K Factor= 5.37 40 18.67 1.101 0.0 1.500 11.112 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 41 18.67 0.0600 0.0 1.500 0.090 Vel = 6.29 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 8 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 41 0.0 1.101 1 E 3.825 3.380 10.552 to 150.0 1 T 9.563 13.387 0.0 29 18.67 0.0599 0.0 16.767 1.004 Vel = 6.29 0.0 18.67 11.556 K Factor= 5.49 42 18.75 1.101 0.0 1.500 11.213 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 43 18.75 0.0607 0.0 1.500 0.091 Vel = 6.32 43 0.0 1.101 1 E 3.825 3.000 10.654 to 150.0 2T 19.125 22.951 0.0 31 18.75 0.0604 0.0 25.951 1.568 Vel = 6.32 0.0 18.75 12.222 K Factor= 5.36 44 20.53 1.101 0.0 1.500 13.439 K Factor= 5.60 to 150.0 0.0 0.0 -0.650 45 20.53 0.0720 0.0 1.500 0.108 Vel = 6.92 45 0.0 1.101 2E 7.65 2.570 12.897 to 150.0 0.0 7.650 0.0 32 20.53 0.0713 0.0 10.220 0.729 Vel = 6.92 0.0 20.53 13.626 K Factor= 5.56 14 10.65 2.003 9E 58.341 338.900 37.865 to 150.0 7T 90.753 149.094 0.0 5 10.65 0.0011 0.0 487.994 0.561 Vel = 1.08 0.0 10.65 38.426 K Factor= 1.72 General Calculation Program Job - THE RESIDENCE AT WINDSOR FARMS Date - 10/21/13 File - C: \HES\HydraCALC\Ver50\Data\Jobs\RES CALC AREA 2 .wxfTime - 12 : 06: 48 AREA CALCULATED - HEAD FLOW SUMMARY Actual Req. Delta Actual Req. Delta ID K-Factor Flow Flow Flow. Press . Press . Press 15 5. 600 14 . 82 14 . 82 0 . 00 7 . 000 Pt 7 . 000 0. 000 22 5. 600 15 . 11 14 . 82 0 .29 7 .277 Pt 7 . 000 0 .277 24 5. 600 15 . 52 14 . 82 0 . 71 7 . 683 Pt 7 . 000 0 . 683 26 5. 600 17 . 70 14 . 82 2 . 88 9. 989 Pt 7 . 000 2 . 989 27 5. 600 18 . 21 15. 90 2 . 31 10 .578 Pt 8 . 062 2 . 516 33 5. 600 18 . 40 14 . 82 3 . 58 10 . 797 Pt 7 . 000 3.797 37 5. 600 18 . 31 14 . 82 3 . 49 10 . 691 Pt 7 . 000 3. 691 38 5. 600 ' 18 . 35 14 . 82 3. 53 10 .732 Pt 7 . 000 3 .732 40 5. 600 18 . 67 14 . 82 3 . 85 11. 112 Pt 7 . 000 4 . 112 42 5. 600 18 . 75 14 . 82 3 . 94 11 .213 Pt 7 . 000 4 .213 44 5. 600 20 . 53 14 . 82 5 . 71 13 . 439 Pt 7 . 000 6. 439 Total K Factors . 11 Total Fixed Flows . . . 0 Sum Actual Flow. . . . 194 . 36 Sum Required Flow. . . 164 . 06 Sum Delta Flow . . . . 30 .30 Max Delta Flow . . . . 5. 71 Max Delta Pressure . . 6. 439 AREA CALCULATED - COMPLETE SUMMARY Start Finish Diam. Start Normal Pf Elev/Fixed Flow Vel Point Point Pres . Pres . 1 Y Pres . 15 <- 16 1 . 101 7 . 000 0. 059 -0 . 650 14 . 82 4 . 99 16 <- 17 1 . 101 6. 409 0 . 867 0 . 000 14 . 82 4 . 99 17 <- 18 1 . 394 7 .276 0 . 439 0 . 000 29 . 92 6.29 18 <- 19 1 .394 7. 715 1 . 944 0 . 000 45. 44 9. 55 19 <- 20 1 . 598 9. 660 0 . 280 0. 000 45. 44 7 .27 20 <- 21 1 . 598 9. 939 1 . 617 0 . 000 63 . 14 10 . 10 21 <- 21A 2 . 003 11 . 557 11 .214 0. 000 92 .70 9 . 44 21A <- R4 2 . 157 22 . 771 1 . 981 3 . 000 92 . 70 8 . 14 R4 <- R3 4 .260 27 . 752 0. 087 9. 961 92 .70 2 . 09 R3 <- 14 4 .260 37 . 800 0 . 065 0 . 000 92 .70 2 . 09 14 <- 6 4 .260 37 . 865 0 . 660 0 . 000 82.. 05 1 . 85 6 <- TOR 4 .260 38 . 525 0 . 441 0 . 000 194 . 36 4 . 38 TOR <- BOR 4 .260 38 . 966 0 . 206 6. 681 194 . 36 4 . 38 BOR <- UG1 4 .260 45. 853 0 . 000 3 .266 194 . 36 4 . 38 UG1 <- UG2 4 . 100 49. 119 0. 177 2 . 599 194 . 36 4 . 72 UG2 <- UG3 4 . 100 51 . 894 0 . 469 0 . 000 194 . 36 4 . 72 UG3 <- TEST 8 .270 52 . 363 0 . 191 -2 . 165 194 . 36 1 . 16 22 <- 23 1 . 101 7 .277 0 . 061 -0 . 650 15. 11 5. 09 23 <- 17 1 . 101 6. 688 0 . 588 0 . 000 15 . 11 15. 09 24 <- 25 1 . 101 7 . 683 0 . 064 -0 . 650 15 . 52 5.23 25 <- 18 1 . 101 7 . 097 0 . 618 0 . 000 15. 52 5.23 26 <- 20 1. 101 9. 989 0. 600 -0 . 650 17 . 70 5. 96 27 <- 28 1 . 101 10. 578 0. 086 -0 . 650 18 .21 6. 14 28 <- 4 1 . 101 10. 014 1 . 496 0 . 000 18 .21 6 . 14 4 <- 29 2 . 003 11 . 510 0 . 046 0 . 000 25 . 37 2 . 58 29 <- 30 2 . 003 11 .557 0 . 114 0 . 000 - 2 f 44 . 04 4 . 48 30 <- 31 2 . 003 11 . 671 0 . 551 0 . 000 62 . 38 6. 35 31 <- 32 2 . 003 12 .222 1 .405 0 . 000 81 . 14 8 .26 32 <- 32A 2 . 003 13. 626 8 . 310 0 . 000 101 . 67 10 . 35 32A <- R2 2 . 157 21. 936 3.349 3 . 000 101 . 67 8 . 93 R2 <- Rl 4 .260 28 .285 0 . 104 9. 961 101 . 67 2 .29 R1 <- 5 4 .260 38 .350 0 . 077 0 .000 101 . 67 2 . 29 5 <- 6 4 .260 38 . 426 0 . 099 0 . 000 112 .32 2 . 53 33 <- 34 1 . 101 10. 797 0 . 087 -0 . 650 18 . 40 6.20 34 G- 35 1 . 101 10 .235 0 . 446 0 . 000 18 . 40 6.20 35 <- 36 1 . 394 10. 681 0 . 820 0 . 000 36. 71 7 . 72 36 <- 21 2 . 003 11 . 501 0 . 056 0 . 000 29. 55 3 . 01 37 <- 35 1 . 101 10. 691 0 . 639 -0 . 650 18 . 31 6. 17 36 <- 4 2 . 003 11 . 501 0 . 009 0 . 000 7. 16 0. 73 38 <- 39 1 . 101 10 . 732 0 . 087 -0 . 650 18 .35 6. 18 39 G- 30 1 . 101 10 . 170 1 . 501 0. 000 18 . 35 6. 18 40 <- 41 1 . 101 11. 112 0 . 090 -0. 650 18 . 67 6.29 41 <- 29 1 . 101 10 . 552 1 . 004 0 . 000 18 . 67 6 .29 42 <- 43 1 . 101 11 .213 0 . 091 -0 . 650 18 . 75 6. 32 43 <- 31 1 . 101 10 . 654 1 . 567 0 . 000 18 .75 6.32 44 G- 45 1 . 101 13. 439 0 . 107 -0 . 650 20 .53 6. 92 45 <- 32 1 . 101 12 . 897 0 . 730 0 . 000 20 . 53 6. 92 14 <- 5 2 . 003 37 . 865 0 . 561 0 . 000 10 . 65 1. 08 Pipe with highest velocity: 32 - 32A (10 . 352) Water Supply Summary @ Point TEST Total Flow From Water Supply Curve . . . . . . . . 294 .363 3 i Pressure From Water Supply Curve . . . . . . . . . 89. 506 System Pressure Demand At Supply Curve . . . . . . 50 . 388 Safety Margin at Supply Curve. . . . . . . . . 39. 118 y 4 Fire Protection by, Computer Design aG� Z UC.NO. n .r i�F ttF i p Df K, ALLSTATE FIRE SYSTEMS 110 MURPHY RD HARTFORD, CT. 06114 860-246-7711 Job Name THE RESIDENCE AT WINDSOR FARMS Building 1ST FLOOR KITCHEN Location 200 DEMING STREET SOUTH WINDSOR, CT. System 3 Contract Data File RES CALC AREA 3.wxf ALLSTATE FIRE SYSTEMS Page 1 THE RESIDENCE AT WINDSOR FARMS Date Hydraulic Design Information Sheet Name - THE RESIDENCE AT WINDSOR FARMS Date - 10/15/13 Location - 200 DEMING STREET SOUTH WINDSOR, CT. Building - 1ST FLOOR KITCHEN System No. - 3 Contractor - ALLSTATE FIRE SYSTEMS Contract No. - Calculated By - PAUL FORAUER Drawing No. - FP-1 Construction: ( ) Combustible (X) Non-Combustible Ceiling Height - 810 Occupancy - ORDINARY HAZARD GROUP 1 S (X) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. (X) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure Curve S Other T Specific Ruling Made By Date E M Area of Sprinkler Operation - 925 System Type Sprinkler/Nozzle Density - .15 (X) Wet Make TYCO D Area Per Sprinkler - 100 ( ) Dry Model RFII E Elevation at Highest Outlet - 10.33 ( ) Deluge Size 1/2" S Hose Allowance - Inside - ( ) Preaction K-Factor 5.6 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.155 G Hose Allowance - Outside - 250 N Note Calculation Flow Required - 458.715 Press Required - 46.793 Summary C-Factor Used: 150 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - 06/06/13 Cap. - T Time of Test - Rated Cap.- Elev.- E Static Press - 90 @ Press - R Residual Press - 70 Elev. - Well Flow - 2176 Proof Flow S Elevation - 0 U P Location - 200 DEMING STREET P L Source of Information - CONTRACT DRAWING FP0.00 Y C Commodity Class Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled % 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 0 C R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse G E Horizontal Barriers Provided: ater Supply Curve (C) LLSTATE FIRE SYSTEMS Page 2 HE RESIDENCE AT WINDSOR FARMS Date City Water Supply: Demand: C1 -Static Pressure 90 D1 - Elevation 3.465 C2 - Residual Pressure: 70 D2-System Flow 208.715 C2- Residual Flow 2176 D2 -System Pressure 46.793 Hose ( Demand ) 250 D3 System Demand 458.715 Safety Margin 42.084 150 140 130 P 120 R 110 E 100 C1 S 90 S 80 C2 U 70 R 60 E 50 40 3 30 20 10 300 600 900 1200 1500 1800 2100 2400 2700 FLOW N ^ 1.85 ) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 fittings Used Summary LLSTATE FIRE SYSTEMS Page 3 rHE RESIDENCE AT WINDSOR FARMS Date -fitting Legend kbbrev. Name '/2 3/4 1 1'/ 1'/2 2 2'/2 3 3'/z 4 5 6 8 10 12 14 16 18 20 24 3 NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 Roll Groove Coupling 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 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 'sp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 * CPVC Tee-Branch 3 3 5 6 8 10 12 15 0 0 0 0 0 0 0 0 0 0 0 0 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 _ib Wilkins 350A Fitting generates a Fixed Loss Based on Flow Jnits Summary )iameter Units Inches .ength Units Feet 'low Units US Gallons per Minute 'ressure Units Pounds per Square Inch Jote: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. _quivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors if 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 :)r 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 ALLSTATE FIRE SYSTEMS Page 4 THE RESIDENCE AT WINDSOR-FARMS Date Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Reg. 46 8.0 5.6 7.17 na 15.0 0.15 100 7.0 47 10.33 6.26 na 48 10.0 7.15 na 49 10.0 8.17 na 50 10.0 9.11 na 51 10.0 10.8 na 52 10.0 17.99 na 14A 9.5 30.08 na 14 9.5 34.22 na 6 9.5 34.67 na TOR 9.5 35.17 na BOR 1.0 42.08 na UG1 1.0 45.41 na UG2 -5.0 48.21 na UG3 -5.0 48.74 na TEST 0.0 46.79 na 250.0 53 8.0 5.6 7.23 na 15.06 0.15 93 7.0 54 10.33 6.32 na 55 10.0 7.21 na 56 8.0 5.6 7.2 na 15.03 0.15 66 7.0 57 10.33 6.28 na 58 8.0 5.6 7.26 na 15.09 0.15 67 7.0 59 10.33 6.34 na 60 8.0 5.6 9.18 na 16.97 0.15 93 7.0 61 10.0 8.41 na 62 8.0 5.6 10.75 na 18.36 0.15 98 7.0 63 10.0 10.0 na 64 10.0 18.09 na 65 10.0 19.3 na 5A 9.5 25.42 na 5 9•5 34.51 na 66 8.0 5.6 9.49 na 17.25 0.15 99 7.0 67 10.33 8.6 na 68 10.0 9.81 na 69 10.0 10.17 na 70 10.0 11.18 na 71 10.0 12.52 na 72 8.0 5.6 9.59 na 17.35 0.15 96 7.0 73 10.33 8.71 .. na 74 8.0 5.6 9.9 na 17.62 0.15 96 7.0 75 10.33 9.02 na 76 8.0 5.6 10.82 na 18.42 0.15 96 7.0 77 10.33 9.95 na 78 &0 5.6 12.03 na 19.42 0.15 72 7.0 79 10.33 11.17 na 80 8.0 5.6 17.1 na 23.16 0.15 96 7.0 81 10.33 16.3 na 82 10.0 18.28 na 83 10.0 18.45 na The maximum velocity is 20.08 and it occurs in the pipe between nodes 51 and 52 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 5 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" - or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 46 15.00 1.101 0.0 2.330 7.175 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 47 15.0 0.0399 0.0 2.330 0.093 Vel = 5.05 47 0.0 1.101 3E 11.475 7.190 6.259 to 150.0 0.0 11.475 0.143 48 15.0 0.0400 0.0 18.665 0.746 Vel = 5.05 48 15.03 1.394 1 E 4.762 8.130 7.148 to 150.0 IT 9.523 14.284 0.0 49 30.03 0.0457 0.0 22.414 1.024 Vel = 6.31 49 30.14 1.394 0.0 5.670 8.172 to 150.0 . 0.0 0.0 0.0 50 60.17 0.1656 0.0 5.670 0.939 Vel = 12.65 50 16.97 1.394 0.0 6.460 9.111 to 150.0 0.0 0.0 0.0 51 77.14 0.2619 0.0 6.460 1.692 Vel = 16.22 51 18.36 1.394 IT 9.523 8.950 10.80.3 to 150.0 0.0 9.523 0.0 52 95.5 0.3889 0.0 18.473 7.184 Vel = 20.08 52 -29.20 2.003 5T 64.823 259.865 17.987 to 150.0 4E 25.929 90.752 0.217 14A 66.3 0.0339 0.0 350.617 11.881 Vel = 6.75 14A 0.0 2.157 2E 12.307 12.125 30.085 to 120.0 1 B 7.384 19.691 3.000 * Fixed loss = 3 14 66.3 0.0357 1 Fsp 0.0 31.816 1.135 Vel = 5.82 14 0.0 4.26 7E 92.17 250.710 34.220 to 120.0 0.0 92.170 0.0 6 66.3 0.0013 0.0 342.880 0.446 Vel = 1.49 6 142.42 4.26 1 E 13.167 33.260 34.666 to 120.0 0.0 13.167 0.0 TOR 208.72 0.0108 0.0 46.427 0.502 Vel = 4.70 TOR 0.0 4.26 1 E 13.167 8.500 35.168 to 120.0 1 Fsp 0.0 13.167 6.681 * Fixed loss = 3 BOR 208.72 0.0108 0.0 21.667 0.235 Vel = 4.70 BOR 0.0 4.26 1Zib 0.0 0.010 42.084 to 120.0 0.0 0.0 3.321 * Fixed loss = 3.321 UG1 208.72 0.1000 0.0 0.010 0.001 Vel = 4.70 UG1 0.0 4.1 1 E 14.534 6.000 45.406 to 140.0 0.0 14.534 2.599 UG2 208.72 0.0098 0.0 20.534 0.201 Vel = 5.07 UG2 0.0 4.1 1 E 14.534 40.000 48.206 to 140.0 0.0 14.534 0.0 UG3 208.72 0.0098 0.0 54.5.34 0.535 Vel = 5.07 UG3 0.0 8.27 4E 113.872 500.000 48.741 to 140.0 1 G 6.326 175.552 -2.166 TEST 208.72 0.0003 1T 55.354 675.552 0.218 Vel = 1.25 250.00 Qa = 250.00 - 458.72 - 46.793 K Factor= 67.06 53 15.06 1.101 0.0 2.330 7.231 K Factor=5.60 to 150.0 0.0 0.0 -1.009 54 15.06 0.0403 0.0 2.330 0.094 Vel = 5.08 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 6 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 54 0.0 1.101 3E 11.475 7.230 6.316 to 150.0 0.0 11.475 0.143 55 15.06 0.0403 0.0 18.705 0.753 Vel = 5.08 55 15.09 1.394 1 E 4.762 6.570 7.212 to 150.0 IT 9.523 14.284 0.0 49 30.15 0.0460 0.0 20.854 0.960 Vel= 6.34 0.0 30.15 8.172 K Factor= 10.55 56 15.03 1.101 0.0 2.330 7.200 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 57 15.03 0.0399 0.0 2.330 0.093 Vel = 5.06 57 0.0 1.101 2E 7.65 0.750 6.284 to 150.0 IT 9.563 17.212 0.143 48 15.03 0.0401 0.0 17.962 0.721 Vel = 5.06 0.0 15.03 7.148 K Factor= 5.62 58 15.09 1.101 0.0 2.330 7.260 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 59 15.09 0.0403 0.0 2.330 0.094 Vel = 5.09 59 0.0 1.101 2E 7.65 0.710 6.345 to 150.0 IT 9.563 17.212 0.143 55 15.09 0.0404 0.0 17.922 0.724 Vel = 5.09 0.0 15.09 7.212 K Factor= 5.62 60 16.97 1.101 0.0 2.000 9.180 K Factor= 5.60 to 150.0 0.0 0.0 -0.866 61 16.97 0.0500 0.0 2.000 0.100 Vel = 5.72 61 0.0 1.101 1 E 3.825 0.500 8.414 to 150.0 1 T 9.563 13.387 0.0 50 16.97 0.0502 0.0 13.887 0.697 Vel = 5.72 0.0 16.97 9.111 K Factor= 5.62 62 18.36 1.101 0.0 2.000 10.747 K Factor= 5.60 to 150.0 0.0 0.0 -0.866 63 18.36 0.0580 0.0 2.000 0.116 Vel = 6.19 63 0.0 1:101 1 E 3.825 0.500 9.997 to 150.0 IT 9.563 13.387 0.0 51 18.36 0.0580 0.0 13.887 0.806 Vel = 6.19 0.0 18.36 10.803 K Factor= 5.59 52 29.19 2.003 0.0 14.350 17.987 to 150.0 0.0 0.0 0.0 64 29.19 0.0074 0.0 14.350 0.106 Vel = 2.97 64 90.07 2.003 0.0 12.000 18.093 to 150.0 0.0 0.0 0.0 65 119.26 0.1004 0.0 12.000 1.205 Vel = 12.14 65 23.15 2.003 1 C 1.296 31.060 19.298 to 150.0 10 10.0 11.296 0.217 5A 142.41 0.1394 0.0 42.356 5.904 Vel = 14.50 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 7 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes ****** Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 5A 0.0 2.157 4E 24.613 9.500 25.419 to 120.0 1 B 7.384 31.997 3.000 * Fixed loss =3 5 142.41 0.1468 1 Fsp 0.0 41.497 6.093 Vel = 12.50 5 0.0 4.26 IT 26.334 2.360 34.512 to 120.0 0.0 26.334 0.0 6 142.41 0.0054 0.0 28.694 0.154 Vel = 3.21 0.0 142.41 34.666 K Factor= 24.19 66 17.25 1.101 0.0 2.330 9.488 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 67 17.25 0.0515 0.0 2.330 0.120 Vel = 5.81 67 0.0 1.101 3E 11.475 9.160 8.599 to 150.0 0.0 11.475 0.143 68 17.25 0.0518 0.0 20.635 1.068 Vel = 5.81 68 17.35 1.394 0.0 6.000 9.810 to 150.0 0.0 0.0 0.0 69 34.6 0.0595 0.0 6.000 0.357 Vel = 7.27 69 17.62 1.394 0.0 8.000 10.167 to 150.0 0.0 0.0 0.0 70 52.22 0.1272 0.0 8.000 1.018 Vel = 10.98 70 18.42 1.394 0.0 6.000 11.185 to 150.0 0.0 0.0 0.0 71 70.64 0.2225 0.0 6.000 1.335 Vel = 14.85 71 19.42 1.394 1T 9.523 6.450 12.520 to 150.0 0.0 9.523 0.0 64 90.06 0.3489 0.0 15.973 5.573 Vel = 18.93 0.0 90.06 18.093 K Factor= 21.17 72 17.35 1.101 0.0 2.330 9.594 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 73 17.35 0.0524 0.0 2.330 0.122 Vel = 5.85 73 0.0 1.101 2E 7.65 1.160 8.707 to 150.0 IT 9.563 17.212 0.143 68 17.35 0.0523 0.0 18.372 0.960 Vel = 5.85 0.0 17.35 9.810 K Factor= 5.54 74 17.62 1.101 0.0 2.330 9.900 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 75 17.62 0.0541 0.0 2.330 0.126 Vel = 5.94 75 0.0 1.101 2E 7.65 1.500 9.017 to 150.0 IT 9.563 17.212 0.143 69 17.62 0.0538 0.0 18.712 1.007 Vel = 5.94 0.0 17.62 10.167 K Factor= 5.53 76 18.42 1.101 0.0 2.330 10.821 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 77 18.42 0.0584 0.0 2.330 0.136 Vel = 6.21 Final Calculations - Hazen-Williams ALLSTATE FIRE SYSTEMS Page 8 THE RESIDENCE AT WINDSOR FARMS Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. 11G. or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 77 0.0 1.101 2E 7.65 1.500 9.948 to 150.0 1 T 9.563 17.212 0.143 70 18.42 0.0585 0.0 18.712 1.094 Vel = 6.21 0.0 18.42 11.185 K Factor= 5.51 78 19.42 1.101 0.0 2.330 12.030 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 79 19.42 0.0648 0.0 2.330 0.151 Vel = 6.54 79 0.0 1.101 2E 7.65 1.500 11.172 to 150.0 1 T 9.563 17.212 0.143 71 19.42 0.0644 0.0 18.712 1.205 Vel = 6.54 0.0 19.42 12.520 K Factor= 5.49 80 23.16 1.101 0.0 2.330 17.098 K Factor= 5.60 to 150.0 0.0 0.0 -1.009 81 23.16 0.0893 0.0 2.330 0.208 Vel = 7.80 81 0.0 1.101 3E 11.475 9.160 16.297 to 150.0 0.0 11.475 0.143 82 23.16 0.0892 0.0 20.635 1.841 Vel = 7.80 82 0.0 1.394 0.0 6.000 18.281 to 150.0 0.0 0.0 0.0 83 23.16 0.0282 0.0 6.000 0.169 Vel = 4.87 83 0.0 1.394 1 T 9.523 20.450 18.450 to 150.0 0.0 9.523 0.0 65 23.16 0.0283 0.0 29.973 0.848 Vel = 4.87 0.0 23.16 19.298 K Factor= 5.27 General Calculation Program Job - THE RESIDENCE AT WINDSOR FARMS Date - 10/21/13 File - C: \HES\HydraCALC\Ver50\Data\Jobs\RES CALC AREA 3 .wxfTime - 12 : 08 : 06 AREA CALCULATED - HEAD FLOW SUMMARY Actual Req. Delta Actual Req. Delta ID K-Factor Flow Flow Flow. Press . Press . Press 46 5. 600 15. 00 15 . 00 0. 00 7 . 175 Pt 7 . 175 0 . 000 53 5. 600 15. 06 14 . 82 0 .24 7 .231 Pt 7 . 000 0 .231 56 5 . 600 15. 03 14 . 82 0 .21 7 . 200 Pt 7 . 000" 0.200 58 5. 600 15. 09 14 . 82 0 .27 7 .260 Pt 7 . 000 0 .260 60 5. 600 16. 97 14 . 82 2 . 15 9. 180 Pt 7 . 000 2 . 180 62 5. 600 18 . 36 14 . 82 3 . 54 10 . 747 Pt 7 . 000 3 . 747 66 5. 600 17 . 25 14 . 85 2 . 40 9. 488 Pt 7 . 032 2 . 456 72 5 . 600 17 .35 14 . 82 2 . 53 9 . 594 Pt 7 . 000 2 . 594 74 5 . 600 17. 62 14 . 82 2 .80 9 . 900 Pt 7 . 000 2 . 900 76 5 . 600 18 . 42 14 . 82 3. 61 10 . 821 Pt 7 . 000 3. 821 78 5 . 600 19 . 42 14 . 82 4 . 61 12 . 030 Pt 7 . 000 5. 030 80 5. 600 23 . 16 14 . 82 8 .34 17 . 098 Pt 7 . 000 10 . 098 Total K Factors. 12 Total Fixed Flows . 0 Sum Actual Flow. . . . 208 . 72 Sum Required Flow. . . 178 . 01 Sum Delta Flow . . . . 30 . 70 Max Delta Flow . . . . 8 . 34 Max Delta Pressure 10 . 098 AREA CALCULATED - COMPLETE SUMMARY Start Finish Diam. . Start Normal Pf 1 Elev/Fixed Flow Vel Point Point Pres . Pres . Pres . 46 <- 47 1 . 101 7 . 175 0 . 093 -1 . 009 1500 5. 05 47 <- 48 1 . 101 6.259 0 . 746 0 . 143 15. 00 5 . 05 48 <- 49 1 . 394 7 . 148 1 . 025 0. 000 30 . 03 6. 31 49 <- 50 1 . 394 8 . 173 0 . 938 0 . 000 60 . 17 12 . 65 50 <- 51 1 .394 9 . 111 1 . 692 0 . 000 77 . 14 16.22 51 <- 52 1 . 394 10 . 803 7 . 184 0. 000 95 . 50 20. 08 52 <- 14A 2 . 003 17 . 987 11 . 881 0 .217 66. 30 6. 75 14A <- 14 2 . 157 30 . 085 1 . 136 3. 000 66. 30 5. 82 14 <- 6 4 . 260 34 . 221 0 . 445 0. 000 66. 30 1 . 49 6 <- TOR 4 . 260 34 . 666 0 . 503 0 . 000 208 . 72 4 . 70 TOR <- BOR 4 . 260 35. 168 0 .235 6. 681 208 . 72 4 . 70 BOR <- UG1 4 . 260 42 . 084 0 . 000 3. 321 208 . 72 4 . 70 UG1 <- UG2 4 . 100 45. 406 0 .201 2 . 599 208 . 72 5. 07 UG2 <- UG3 4 . 100 48 .206 0 . 535 0 . 000 208 . 72 5. 07 UG3 <- TEST 8 . 270 48 . 741 0 .217 -2 . 165 208 . 72 1 .25 53 <- 54 1 . 101 7 .231 0 . 094 -1 . 009 15. 06 5. 07 54 <- 55 1 . 101 6. 316 0 . 753 0 . 143 15 . 06 5. 07 55 <- 49 1 . 394 7 .212 0 . 961 0. 000 30 . 15 6. 34 56 <- 57 1 . 101 7 .200 0 . 093 -1. 009 15 . 03 5. 06 57 <- 48 1 . 101 6.284 0 . 720 0 . 143 15. 03 5. 06 58 <- 59 1 . 101 7 . 260 0 . 094 -1. 009 15. 09 5. 08 59 <- 55 1 . 101 6. 345 0 .724 0 . 143 15 . 09 5. 08 60 <- 61 1 . 101 9. 180 0 . 100 -0. 866 16. 97 5.72 61 <- 50 1 . 101 8 . 414 0 . 697 0. 000 16. 97 5. 72 62 <- 63 1 . 101 10 . 747 0 . 116 -0 . 866 2 18 . 36 6. 19 63 <- 51 1 . 101 9. 997 0 . 806 0.000 18 . 36 6. 19 52 <- 64 2 . 003 17 . 987 0 . 107 0 .000 29. 19 2 . 97 64 <- 65 2 . 003 18 . 093 1 .205 0 .000 119.26 12 . 14 65 <- 5A 2 . 003 19.298 5. 904 0 .217 142 . 41 14 . 50 5A <- 5 2 . 157 25. 419 6. 094 3. 000 142 . 41 12 .50 5 <- 6 4 .260 34 .512 0 . 153 0.000 142 . 41 3. 21 66 <- 67 1 . 101 9. 488 0 . 121 -1 . 009 17 . 25 5. 81_ 67 <- 68 1. 101 8 . 599 1 . 068 0. 143 17 . 25 5. 81 68 <- 69 1 . 394 9. 810 0 .357 0 . 000 34 . 59 7 .27 69 <- 70 1 . 394 10. 167 1 . 018 0 . 000 52 .22 10 . 98 70 <- 71 1 . 394 11. 185 1 . 336 0 .000 70 . 64 14 .85 71 <- 64 1 . 394 12. 521 5. 573 0 . 000 90. 06 18 . 93 72 <- 73 1 . 101 9.594 0 . 122 -1 . 009 17 . 35 5. 85 73 <- 68 1 . 101 8 . 707 0 . 961 0. 143 17 . 35 5. 85 74 < 75 1 . 101 9. 900 0 . 125 -1. 009 17 . 62 5. 94 75 <- 69 1 . 101 9. 017 1 . 007 0 . 143 17 . 62 5. 94 76 <- 77 1 . 101 10. 821 0 . 136 -1. 009 18 . 42 6.21 77 <- 70 1 . 101 9. 948 1 . 094 0. 143 18 . 42 6. 21 78 <- 79 1 . 101 12 . 030 0 . 150 -1 . 009 19. 42 6. 55 79 <- 71 1 . 101 11. 171 1 .206 0. 143 19 . 42 6. 55 80 <- 81 1 . 101 17 . 098 0 . 208 -1. 009 23 . 16 7 . 80 81 <- 82 1 . 101 16.297 1 . 841 0 . 143 23 . 16 7 . 80 82 <- 83 1 .394 18 .281 0 . 170 0. 000 23 . 16 4 . 87 83 <- 65 1 . 394 18 . 451 0 . 848 0 . 000 23. 16 4 . 87 Pipe with highest velocity: 51 - 52 (20 . 075) 3 Water Supply Summary @ Point TEST Total Flow From Water Supply Curve . . . . . . . . 458 . 715 Pressure From Water Supply Curve . . . . . . . . . 88 . 877 System Pressure Demand At Supply Curve . . . . . . 46. 793 Safety Margin at Supply Curve. . . . . . . 42 . 084. 4