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HYD6 DALAND 3RD FLOOR
METRO - SWIFT SPRINKLER CORP LIC NO SC001199 58r PULASKI ST PEABODY MA 01960 978-532-2907 Job Name : DALAND 3RD FLOOR Remote Area : .10 GPM OVER 1006 SF LH Head Info : 11 CALCULATED @ 120 SF MAX Flows : 438 GPM RQD INCL 250 HOSE Pressures : 45 PSI RQD AT STREET‚ 34 SAFETY Data File : DALAND 3RD FLOOR AREA 6.WXF Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORPPage 1 DALAND 3RD FLOORDate 7-2-2019 10203040E50R60U70S80S90E100R110P120130140150200 400 600 800 1000 1200 1400 1600 1800FLOW ( N ^ 1.85 )City Water Supply:Demand:C1C2C1 - Static Pressure : 79 C2 - Residual Pressure: 76 C2 - Residual Flow : 1350 D1 - Elevation : 18.948 D2 - System Flow : 187.937 D2 - System Pressure : 44.566 Hose ( Demand ) : 250 D3 - System Demand : 437.937 Safety Margin : 34.060 D1D2D3Water Supply Curve CComputer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORPPage 2 DALAND 3RD FLOORDate 7-2-2019 Fitting Legend Abbrev.Name ½¾11¼1½22½33½456810121416182024 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 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 G NFPA 13 Gate Valve 00000111122345678101113 S NFPA 13 Swing Check 0 0 5 7 9 11141619222732455565 T NFPA 13 90' Flow thru Tee 3 4 5 6 8 10121517202530355060718191101121 Zca Colt C200 Horz Butt 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. Fittings Used SummaryComputer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 3 DALAND 3RD FLOOR Date 7-2-2019 Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Req. 300 71.5 5.6 7.0 na 14.82 0.1 120 7.0 301 71.5 5.6 7.75 na 15.59 0.1 120 7.0 302 71.5 5.6 8.58 na 16.4 0.1 120 7.0 303 71.5 5.6 9.91 na 17.63 0.1 120 7.0 304 71.5 5.6 11.32 na 18.84 0.1 120 7.0 315 71.5 13.41 na 316 71.5 13.65 na 317 71.5 14.33 na 318 71.5 16.21 na S4 62.167 22.12 na S3 31.333 35.87 na S2 31.333 36.15 na FB 31.333 36.32 na TOR 31.333 36.35 na BOR 27.333 38.11 na BKFL 27.333 44.66 na UG 24.417 45.95 na TEST 27.75 44.57 na 250.0 305 71.5 5.6 7.13 na 14.96 0.1 120 7.0 306 71.5 5.6 7.89 na 15.73 0.1 120 7.0 307 71.5 5.6 8.74 na 16.55 0.1 120 7.0 308 71.5 5.6 10.1 na 17.79 0.1 120 7.0 309 71.5 5.6 11.53 na 19.01 0.1 120 7.0 310 71.5 5.6 13.55 na 20.62 0.1 120 7.0 The maximum velocity is 13.25 and it occurs in the pipe between nodes 309 and 316 Pressure / Flow Summary - STANDARD Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 4 DALAND 3RD FLOOR Date 7-2-2019 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf *EQUIVALENT K'S *REMOTE HEAD TO SUPPLY 300 71.500 5.60 14.82 1 0.0 10.000 120 7.000 to 0.0 0.0 0.0 301 71.500 14.82 1.049 0.0 10.000 0.0747 0.747 Vel = 5.50 301 71.500 5.60 15.58 1.25 0.0 11.167 120 7.747 to 0.0 0.0 0.0 302 71.500 30.4 1.38 0.0 11.167 0.0742 0.829 Vel = 6.52 302 71.500 5.60 16.40 1.25 0.0 8.083 120 8.576 to 0.0 0.0 0.0 303 71.500 46.8 1.38 0.0 8.083 0.1650 1.334 Vel = 10.04 303 71.500 5.60 17.63 1.5 0.0 10.000 120 9.910 to 0.0 0.0 0.0 304 71.500 64.43 1.61 0.0 10.000 0.1407 1.407 Vel = 10.15 304 71.500 5.60 18.84 1.5 T 8.0 1.250 120 11.317 to 0.0 8.000 0.0 315 71.500 83.27 1.61 0.0 9.250 0.2261 2.091 Vel = 13.12 315 71.500 0.0 2.5 0.0 12.000 120 13.408 to 0.0 0.0 0.0 316 71.500 83.27 2.635 0.0 12.000 0.0206 0.247 Vel = 4.90 316 71.500 84.05 2.5 0.0 9.000 120 13.655 to 0.0 0.0 0.0 317 71.500 167.32 2.635 0.0 9.000 0.0747 0.672 Vel = 9.84 317 71.500 20.62 2.5 T 16.474 3.875 120 14.327 to 0.0 16.474 0.0 318 71.500 187.94 2.635 0.0 20.349 0.0925 1.883 Vel = 11.06 318 71.500 0.0 2.5 E 8.237 11.958 120 16.210 to 0.0 8.237 4.042 S4 62.167 187.94 2.635 0.0 20.195 0.0925 1.869 Vel = 11.06 S4 62.167 0.0 4 E 13.167 30.833 120 22.121 to 0.0 13.167 13.354 S3 31.333 187.94 4.26 0.0 44.000 0.0089 0.393 Vel = 4.23 S3 31.333 0.0 4 T 26.334 5.083 120 35.868 to 0.0 26.334 0.0 S2 31.333 187.94 4.26 0.0 31.417 0.0089 0.280 Vel = 4.23 S2 31.333 0.0 6 T 37.72 28.750 120 36.148 to E 17.603 108.131 0.0 FB 31.333 187.94 6.357 B 12.573 136.881 0.0013 0.174 Vel = 1.90 S 40.235 FB 31.333 0.0 6 E 17.603 3.167 120 36.322 to 0.0 17.603 0.0 TOR 31.333 187.94 6.357 0.0 20.770 0.0013 0.026 Vel = 1.90 TOR 31.333 0.0 6 E 17.603 4.000 120 36.348 to 0.0 17.603 1.732 BOR 27.333 187.94 6.357 0.0 21.603 0.0013 0.028 Vel = 1.90 BOR 27.333 0.0 8 Zca 0.0 7.667 120 38.108 to 0.0 0.0 6.553 * * Fixed Loss = 6.553 BKFL 27.333 187.94 8.249 0.0 7.667 0.0004 0.003 Vel = 1.13 Final Calculations - Hazen-Williams - 2007 Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 5 DALAND 3RD FLOOR Date 7-2-2019 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf BKFL 27.333 0.0 8 3E 63.423 8.833 120 44.664 to 0.0 63.423 1.263 UG 24.417 187.94 8.249 0.0 72.256 0.0004 0.026 Vel = 1.13 UG 24.417 0.0 8 T 41.62 71.000 120 45.953 to G 4.757 89.186 -1.444 TEST 27.75 187.94 8.27 2E 42.809 160.186 0.0004 0.057 Vel = 1.12 250.00 Qa = 250.00 TEST 437.94 44.566 K Factor = 65.60 * 305 71.500 5.60 14.96 1 0.0 10.000 120 7.134 to 0.0 0.0 0.0 306 71.500 14.96 1.049 0.0 10.000 0.0760 0.760 Vel = 5.55 306 71.500 5.60 15.73 1.25 0.0 11.167 120 7.894 to 0.0 0.0 0.0 307 71.500 30.69 1.38 0.0 11.167 0.0756 0.844 Vel = 6.58 307 71.500 5.60 16.56 1.25 0.0 8.083 120 8.738 to 0.0 0.0 0.0 308 71.500 47.25 1.38 0.0 8.083 0.1679 1.357 Vel = 10.14 308 71.500 5.60 17.79 1.5 0.0 10.000 120 10.095 to 0.0 0.0 0.0 309 71.500 65.04 1.61 0.0 10.000 0.1432 1.432 Vel = 10.25 309 71.500 5.60 19.01 1.5 T 8.0 1.250 120 11.527 to 0.0 8.000 0.0 316 71.500 84.05 1.61 0.0 9.250 0.2301 2.128 Vel = 13.25 0.0 316 84.05 13.655 K Factor = 22.75 * 310 71.500 5.60 20.62 1 T 5.0 0.625 120 13.552 to 0.0 5.000 0.0 317 71.500 20.62 1.049 0.0 5.625 0.1378 0.775 Vel = 7.65 0.0 317 20.62 14.327 K Factor = 5.45 Final Calculations - Hazen-Williams Computer Programs by Hydratec Inc. Revision: 50.52.1