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HYD3 PLUMMER HALL READING ROOMMETRO - SWIFT SPRINKLER CORP LIC NO SC001199 58r PULASKI ST PEABODY MA 01960 978-532-2907 Job Name : PLUMMER HALL READING RM PEM Remote Area : .10 GPM OVER 1963 SF - LH Head Info : 14 CALCULATED @ 218 SF MAX Flows : 554 GPM RQD INCL 250 HOSE Pressures : 61 PSI RQD AT STREET - 17 SAFETY Data File : PEM PLUMMER HALL READING RM AREA 3.WXF Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORPPage 1 PLUMMER HALL READING RM PEMDate 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 : 23.820 D2 - System Flow : 303.638 D2 - System Pressure : 60.623 Hose ( Demand ) : 250 D3 - System Demand : 553.638 Safety Margin : 17.801 D1D2D3Water Supply Curve CComputer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORPPage 2 PLUMMER HALL READING RM PEMDate 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 D Dry Rel D28 47 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 PLUMMER HALL READING RM PEM Date 7-2-2019 Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Req. 1 77.875 5.6 11.51 na 19.0 0.1 190 7.0 E1 78.625 11.93 na 2 74.667 5.6 15.15 na 21.8 0.1 218 7.0 E2 77.5 16.16 na 3 81.292 5.6 12.0 na 19.4 0.1 194 7.0 E3 82.75 12.68 na 4 81.292 5.6 12.0 na 19.4 0.1 194 7.0 E4 82.75 12.73 na 5 81.292 5.6 11.51 na 19.0 0.1 190 7.0 E5 82.75 11.84 na 142 74.667 5.6 18.98 na 24.4 0.1 218 7.0 D18 77.5 20.49 na D17 77.5 20.5 na D16 77.5 20.5 na D15 77.5 20.5 na D14 77.5 20.5 na D13 77.5 20.51 na D12 77.5 20.55 na D11 77.5 20.57 na D10 77.5 20.58 na D9 77.5 20.67 na D8 77.5 20.71 na D7 77.5 20.72 na D6 77.5 20.87 na D5 77.5 20.95 na D4 77.5 21.01 na D3 77.5 22.24 na D2 77.5 22.85 na D1 77.5 23.52 na TDR 77.5 23.95 na BDR 72.583 27.71 na F3 72.583 28.75 na FM 63.542 32.86 na F2 46.333 41.58 na F1 31.333 50.13 na FB 31.333 55.36 na TOR 31.333 55.42 na BOR 27.333 57.22 na BKFL 27.333 60.6 na UG 24.417 61.93 na TEST 27.75 60.62 na 250.0 141 78.625 K = K @ E1 18.59 na 23.72 104 82.75 12.68 na 143 82.75 K = K @ E3 12.68 na 19.4 144 82.75 K = K @ E3 13.06 na 19.69 105 82.75 13.49 na 106 80.0 17.73 na 110 82.75 12.74 na 147 82.75 K = K @ E3 12.74 na 19.44 148 82.75 K = K @ E3 13.12 na 19.73 111 82.75 13.54 na 112 80.0 17.8 na 115 82.75 12.84 na 149 82.75 K = K @ E4 12.84 na 19.49 150 82.75 K = K @ E4 13.23 na 19.78 116 82.75 13.65 na 117 80.0 17.92 na 121 82.75 12.9 na 152 82.75 K = K @ E5 12.9 na 19.82 153 82.75 K = K @ E5 13.29 na 20.13 122 82.75 13.73 na Pressure / Flow Summary - STANDARD Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 4 PLUMMER HALL READING RM PEM Date 7-2-2019 Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Req. 123 80.0 18.1 na 145 74.667 5.6 18.99 na 24.4 0.1 218 7.0 146 74.667 5.6 19.04 na 24.44 0.1 218 7.0 151 74.667 5.6 19.18 na 24.53 0.1 218 7.0 154 74.667 5.6 19.44 na 24.69 0.1 218 7.0 The maximum velocity is 9.17 and it occurs in the pipe between nodes 154 and D4 Flow Summary - Standard Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 5 PLUMMER HALL READING RM PEM 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 1 77.875 5.60 19.00 1 T 3.568 0.917 100 11.512 to 0.0 3.568 -0.325 E1 78.625 19.0 1.049 0.0 4.485 0.1657 0.743 Vel = 7.05 0.0 E1 19.00 11.930 K Factor = 5.50 * 2 74.667 5.60 21.80 1 T 3.568 4.000 100 15.154 to 2E 2.855 6.423 -1.227 E2 77.500 21.8 1.049 0.0 10.423 0.2139 2.229 Vel = 8.09 0.0 E2 21.80 16.156 K Factor = 5.42 * 3 81.292 5.60 19.40 1 T 3.568 2.625 100 12.001 to E 1.427 4.995 -0.631 E3 82.750 19.4 1.049 0.0 7.620 0.1723 1.313 Vel = 7.20 0.0 E3 19.40 12.683 K Factor = 5.45 * 4 81.292 5.60 19.40 1 T 3.568 2.875 100 12.001 to E 1.427 4.995 -0.631 E4 82.750 19.4 1.049 0.0 7.870 0.1723 1.356 Vel = 7.20 0.0 E4 19.40 12.726 K Factor = 5.44 * 5 81.292 5.60 19.00 1 T 3.568 2.250 100 11.512 to 0.0 3.568 -0.631 E5 82.750 19.0 1.049 0.0 5.818 0.1657 0.964 Vel = 7.05 0.0 E5 19.00 11.845 K Factor = 5.52 * *REMOTE HEAD TO SUPPLY 142 74.667 5.60 24.40 1 T 3.568 4.000 100 18.977 to 2E 2.855 6.423 -1.227 D18 77.500 24.4 1.049 0.0 10.423 0.2634 2.745 Vel = 9.06 D18 77.500 0.0 4 0.0 1.875 100 20.495 to 0.0 0.0 0.0 D17 77.500 24.4 4.26 0.0 1.875 0 0.0 Vel = 0.55 D17 77.500 0.0 4 0.0 2.542 100 20.495 to 0.0 0.0 0.0 D16 77.500 24.4 4.26 0.0 2.542 0.0004 0.001 Vel = 0.55 D16 77.500 23.71 4 0.0 4.458 100 20.496 to 0.0 0.0 0.0 D15 77.500 48.11 4.26 0.0 4.458 0.0009 0.004 Vel = 1.08 D15 77.500 0.0 4 0.0 3.958 100 20.500 to 0.0 0.0 0.0 D14 77.500 48.11 4.26 0.0 3.958 0.0010 0.004 Vel = 1.08 Final Calculations - Hazen-Williams - 2007 Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 6 PLUMMER HALL READING RM PEM 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 D14 77.500 24.40 4 0.0 1.833 100 20.504 to 0.0 0.0 0.0 D13 77.500 72.51 4.26 0.0 1.833 0.0022 0.004 Vel = 1.63 D13 77.500 39.09 4 0.0 8.833 100 20.508 to 0.0 0.0 0.0 D12 77.500 111.6 4.26 0.0 8.833 0.0048 0.042 Vel = 2.51 D12 77.500 0.0 4 0.0 3.833 100 20.550 to 0.0 0.0 0.0 D11 77.500 111.6 4.26 0.0 3.833 0.0050 0.019 Vel = 2.51 D11 77.500 24.44 4 0.0 1.833 100 20.569 to 0.0 0.0 0.0 D10 77.500 136.04 4.26 0.0 1.833 0.0065 0.012 Vel = 3.06 D10 77.500 39.17 4 0.0 8.167 100 20.581 to 0.0 0.0 0.0 D9 77.500 175.21 4.26 0.0 8.167 0.0110 0.090 Vel = 3.94 D9 77.500 0.0 4 0.0 3.792 100 20.671 to 0.0 0.0 0.0 D8 77.500 175.21 4.26 0.0 3.792 0.0108 0.041 Vel = 3.94 D8 77.500 39.26 4 0.0 0.750 100 20.712 to 0.0 0.0 0.0 D7 77.500 214.47 4.26 0.0 0.750 0.0160 0.012 Vel = 4.83 D7 77.500 24.53 4 0.0 7.625 100 20.724 to 0.0 0.0 0.0 D6 77.500 239.0 4.26 0.0 7.625 0.0195 0.149 Vel = 5.38 D6 77.500 0.0 4 0.0 3.875 100 20.873 to 0.0 0.0 0.0 D5 77.500 239.0 4.26 0.0 3.875 0.0196 0.076 Vel = 5.38 D5 77.500 39.95 4 0.0 2.542 100 20.949 to 0.0 0.0 0.0 D4 77.500 278.95 4.26 0.0 2.542 0.0260 0.066 Vel = 6.28 D4 77.500 24.69 4 3E 28.192 12.125 100 21.015 to 0.0 28.192 0.0 D3 77.500 303.64 4.26 0.0 40.317 0.0303 1.223 Vel = 6.83 D3 77.500 0.0 4 0.0 20.042 100 22.238 to 0.0 0.0 0.0 D2 77.500 303.64 4.26 0.0 20.042 0.0304 0.609 Vel = 6.83 D2 77.500 0.0 4 T 18.795 3.250 100 22.847 to 0.0 18.795 0.0 D1 77.500 303.64 4.26 0.0 22.045 0.0303 0.669 Vel = 6.83 D1 77.500 0.0 4 E 9.397 5.000 100 23.516 to 0.0 9.397 0.0 TDR 77.500 303.64 4.26 0.0 14.397 0.0304 0.437 Vel = 6.83 TDR 77.500 0.0 4 D 19.984 4.917 100 23.953 to B 8.564 35.685 2.130 BDR 72.583 303.64 4.026 E 7.137 40.602 0.0400 1.623 Vel = 7.65 BDR 72.583 0.0 4 T 26.334 8.667 120 27.706 to E 13.167 39.501 0.0 F3 72.583 303.64 4.26 0.0 48.168 0.0217 1.043 Vel = 6.83 Final Calculations - Hazen-Williams Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 7 PLUMMER HALL READING RM PEM 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 F3 72.583 0.0 4 0.0 9.042 120 28.749 to 0.0 0.0 3.916 FM 63.542 303.64 4.26 0.0 9.042 0.0217 0.196 Vel = 6.83 FM 63.542 0.0 4 T 26.334 18.917 120 32.861 to E 13.167 39.501 7.453 F2 46.333 303.64 4.26 0.0 58.418 0.0217 1.266 Vel = 6.83 F2 46.333 0.0 4 T 26.334 28.917 120 41.580 to 3E 39.501 65.835 6.496 F1 31.333 303.64 4.26 0.0 94.752 0.0217 2.053 Vel = 6.83 F1 31.333 0.0 4 2T 52.668 64.958 120 50.129 to 6E 79.002 176.438 0.0 FB 31.333 303.64 4.26 B 15.8 241.396 0.0217 5.231 Vel = 6.83 S 28.968 FB 31.333 0.0 6 E 17.603 3.167 120 55.360 to 0.0 17.603 0.0 TOR 31.333 303.64 6.357 0.0 20.770 0.0031 0.064 Vel = 3.07 TOR 31.333 0.0 6 E 17.603 4.000 120 55.424 to 0.0 17.603 1.732 BOR 27.333 303.64 6.357 0.0 21.603 0.0031 0.067 Vel = 3.07 BOR 27.333 0.0 8 Zca 0.0 7.667 120 57.223 to 0.0 0.0 3.374 * * Fixed Loss = 3.374 BKFL 27.333 303.64 8.249 0.0 7.667 0.0008 0.006 Vel = 1.82 BKFL 27.333 0.0 8 3E 63.423 8.833 120 60.603 to 0.0 63.423 1.263 UG 24.417 303.64 8.249 0.0 72.256 0.0009 0.063 Vel = 1.82 UG 24.417 0.0 8 T 41.62 71.000 120 61.929 to G 4.757 89.186 -1.444 TEST 27.75 303.64 8.27 2E 42.809 160.186 0.0009 0.138 Vel = 1.81 250.00 Qa = 250.00 TEST 553.64 60.623 K Factor = 71.11 * 141 78.625 5.5 23.72 1.25 T 4.282 13.042 100 18.588 K = K @ E1 to 2E 4.282 8.564 0.487 D16 77.500 23.72 1.38 0.0 21.606 0.0658 1.421 Vel = 5.09 0.0 D16 23.72 20.496 K Factor = 5.24 * 104 82.750 0.0 1.25 0.0 2.375 100 12.683 to 0.0 0.0 0.0 143 82.750 0.0 1.38 0.0 2.375 0 0.0 Vel = 0 143 82.750 5.45 19.40 1.25 0.0 8.417 100 12.683 K = K @ E3 to 0.0 0.0 0.0 144 82.750 19.4 1.38 0.0 8.417 0.0454 0.382 Vel = 4.16 144 82.750 5.45 19.69 1.25 0.0 2.542 100 13.065 K = K @ E3 to 0.0 0.0 0.0 105 82.750 39.09 1.38 0.0 2.542 0.1656 0.421 Vel = 8.38 105 82.750 0.0 1.25 2E 4.282 14.167 100 13.486 to 0.0 4.282 1.191 106 80 39.09 1.38 0.0 18.449 0.1656 3.056 Vel = 8.38 Final Calculations - Hazen-Williams Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 8 PLUMMER HALL READING RM PEM 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 106 80 0.0 1.25 T 4.282 3.792 100 17.733 to E 2.141 6.423 1.083 D13 77.500 39.09 1.38 0.0 10.215 0.1656 1.692 Vel = 8.38 0.0 D13 39.09 20.508 K Factor = 8.63 * 110 82.750 0.0 1.25 0.0 2.375 100 12.735 to 0.0 0.0 0.0 147 82.750 0.0 1.38 0.0 2.375 0 0.0 Vel = 0 147 82.750 5.45 19.44 1.25 0.0 8.417 100 12.735 K = K @ E3 to 0.0 0.0 0.0 148 82.750 19.44 1.38 0.0 8.417 0.0455 0.383 Vel = 4.17 148 82.750 5.45 19.73 1.25 0.0 2.542 100 13.118 K = K @ E3 to 0.0 0.0 0.0 111 82.750 39.17 1.38 0.0 2.542 0.1664 0.423 Vel = 8.40 111 82.750 0.0 1.25 2E 4.282 14.167 100 13.541 to 0.0 4.282 1.191 112 80 39.17 1.38 0.0 18.449 0.1663 3.068 Vel = 8.40 112 80 0.0 1.25 T 4.282 3.792 100 17.800 to E 2.141 6.423 1.083 D10 77.500 39.17 1.38 0.0 10.215 0.1662 1.698 Vel = 8.40 0.0 D10 39.17 20.581 K Factor = 8.63 * 115 82.750 0.0 1.25 0.0 2.375 100 12.841 to 0.0 0.0 0.0 149 82.750 0.0 1.38 0.0 2.375 0 0.0 Vel = 0 149 82.750 5.44 19.49 1.25 0.0 8.417 100 12.841 K = K @ E4 to 0.0 0.0 0.0 150 82.750 19.49 1.38 0.0 8.417 0.0457 0.385 Vel = 4.18 150 82.750 5.44 19.77 1.25 0.0 2.542 100 13.226 K = K @ E4 to 0.0 0.0 0.0 116 82.750 39.26 1.38 0.0 2.542 0.1668 0.424 Vel = 8.42 116 82.750 0.0 1.25 2E 4.282 14.167 100 13.650 to 0.0 4.282 1.191 117 80 39.26 1.38 0.0 18.449 0.1671 3.082 Vel = 8.42 117 80 0.0 1.25 T 4.282 3.792 100 17.923 to E 2.141 6.423 1.083 D8 77.500 39.26 1.38 0.0 10.215 0.1670 1.706 Vel = 8.42 0.0 D8 39.26 20.712 K Factor = 8.63 * 121 82.750 0.0 1.25 0.0 2.375 100 12.895 to 0.0 0.0 0.0 152 82.750 0.0 1.38 0.0 2.375 0 0.0 Vel = 0 152 82.750 5.52 19.82 1.25 0.0 8.417 100 12.895 K = K @ E5 to 0.0 0.0 0.0 153 82.750 19.82 1.38 0.0 8.417 0.0472 0.397 Vel = 4.25 Final Calculations - Hazen-Williams Computer Programs by Hydratec Inc. Revision: 50.52.1 METRO - SWIFT SPRINKLER CORP Page 9 PLUMMER HALL READING RM PEM 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 153 82.750 5.52 20.13 1.25 0.0 2.542 100 13.292 K = K @ E5 to 0.0 0.0 0.0 122 82.750 39.95 1.38 0.0 2.542 0.1727 0.439 Vel = 8.57 122 82.750 0.0 1.25 2E 4.282 14.167 100 13.731 to 0.0 4.282 1.191 123 80 39.95 1.38 0.0 18.449 0.1725 3.182 Vel = 8.57 123 80 0.0 1.25 T 4.282 3.792 100 18.104 to E 2.141 6.423 1.083 D5 77.500 39.95 1.38 0.0 10.215 0.1725 1.762 Vel = 8.57 0.0 D5 39.95 20.949 K Factor = 8.73 * 145 74.667 5.60 24.40 1 T 3.568 4.000 100 18.986 to 2E 2.855 6.423 -1.227 D14 77.500 24.4 1.049 0.0 10.423 0.2634 2.745 Vel = 9.06 0.0 D14 24.40 20.504 K Factor = 5.39 * 146 74.667 5.60 24.44 1 T 3.568 4.000 100 19.042 to 2E 2.855 6.423 -1.227 D11 77.500 24.44 1.049 0.0 10.423 0.2642 2.754 Vel = 9.07 0.0 D11 24.44 20.569 K Factor = 5.39 * 151 74.667 5.60 24.53 1 T 3.568 4.000 100 19.180 to 2E 2.855 6.423 -1.227 D7 77.500 24.53 1.049 0.0 10.423 0.2659 2.771 Vel = 9.11 0.0 D7 24.53 20.724 K Factor = 5.39 * 154 74.667 5.60 24.69 1 T 3.568 4.000 100 19.436 to 2E 2.855 6.423 -1.227 D4 77.500 24.69 1.049 0.0 10.423 0.2692 2.806 Vel = 9.17 0.0 D4 24.69 21.015 K Factor = 5.39 * Final Calculations - Hazen-Williams Computer Programs by Hydratec Inc. Revision: 50.52.1