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HomeMy WebLinkAboutWater Report EXti 6%y 13 a College Station Utilities Reliable, Affordable, Community Owned Date Wednesday. July 02. 2008 Time 1'45 Test completed by Matthew Matcek Witness /baron Matthews Location Castlerock Ph 2A Nozzle size 2_5 Flow hydrant R -057 Pitot reading 60 G.P.M. 1300 Static hydrant $ -056 Static PSI L Residual PSI 94 Comments 11_1111A ,- -'.Y4. b( T I-- p..3 1 FLOATE I5 EXPRESSED IN GPM AND PRESSURE IN PS G OUT WR A SUMMARY OF THE ORIGINAL DATA FOLLOWS 0 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 1 1 2 (FEET) 19.0 (INCHES) 0 150.0 .00 2 2 3 307.0 8.0 150.0 .00 3 3 4 95.0 8.0 150.0 .00 4 4 5 280.0 8.0 150.0 .00 5 5 6 283.0 8.0 150.0 .00 6 6 7 321.0 8.0 150.0 .00 7 7 8 165.0 8.0 150.0 .00 8 8 9 34.0 8.0 150.0 .00 10 10 10 336.0 35.0 8.0 150.0 .00 11 11 2 702.0 6.0 150.0 .00 12 10 12 129.0 8.0 150.0 .00 13 7 13 184.0 4.0 150.0 .00 14 6 14 186.0 4.0 150.0 .00 15 5 15 124.0 6.0 150.0 .00 16 15 16 356.0 4.0 150.0 .00 17 3 17 12.0 8.0 150.0 .00 18 17 18 488.0 8.0 150.0 .00 20 19 19 517.0 8.0 150.0 .00 21 12 21 106.0 8.0 150.0 .00 22 21 22 61.0 8.0 150.0 .00 23 22 23 456.0 6.0 150.0 .00 24 23 24 469.0 6.0 150.0 .00 25 22 25 632.0 8.0 150.0 .00 26 25 26 421.0 8.0 150.0 .00 27 26 24 240.0 8.0 150.0 .00 28 24 1 270.0 8.0 150.0 .00 29 0 1 1.0 8.0 150.0 .00 + 517.50 A SUCCESSFUL GEOMETRIC VERIFICATION HAS SEEN COMPLETED °JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES 1 .00 287.00 1 28 29 2 19.50 286.00 1 2 11 3 .00 284.00 2 3 17 4 36.00 283.00 3 4 5 10.50 281,00 4 5 15 6 10.50 282.00 5 6 14 7 9.00 282•.00 6 7 13 8 1.50 282 -.00 7 8 9 7.50 282,00 8 9 10 12.00 286.00 9 10 12 11 24.00 287.00 10 11 12 .00 287.00 12 21 13 6.00 279.00 13 14 12.00 279.00 14 15 12.00 281.00 15 16 16 13.50 279.00 16 17 .00 284.00 17 18 18 .00 284.00 18 19 19 .00 284.00 19 20 20 .00 282.00 20 21 .00 288.00 21 22 22 27.00 288.00 22 23 25 23 24.00 290:00 23 24 24 12.00 291:00 24 27 28 25 31.50 294.00 25 26 26 12.00 297.00 26 27 OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD 0 TH15 SYSTEM HAS 29 PIPES WITH 26 JUNCTIONS , 3 LOOPS AND 1 FGNS 1 THE RESULTS ARE OBTAINED AFTER 6 TRIALS WITH AN ACCURACY s .00246 Ocastle Rock Phases 7 & B 06/07/10 Pile CR78A ]NH Proposed water system w/ FGN (100 psi, 517.5' ms1) 0 castle Rock Dr. 8" WL (FH7) Peak Demand of 1.5 gpni /con (187 cons) 0 PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY H1 /1000 1 1 2 165.86 .01 .00 .00 1.06 .50 2 2 3 104.54 .07 .00 .00 .67 .21 Page 1 I 1 ri� [7 -q ty • CR78A.OUT 3 3 4 104.54 .02 .00 .00 .67 .21 4 4 5 68.54 .03 .00 .00 .44 .10 5 5 6 32.54 .01 .00 .00 .21 .02 6 6 7 10.04 .00 .00 .00 .06 .00 7 7 8 -4.96 .00 .00 .00 -.03 .00 8 8 9 -6.46 .00 .00 .00 -.04 .00 9 9 10 -13.96 .00 .00 .00 -.09 -.01 10 10 11 -17.81 -.01 .00 .00 -.20 -.03 11 11 2 -41.81 -.11 .00 .00 -.47 -.16 12 10 12 -8.14 .00 .00 .00 -.05 .00 13 7 13 6.00 .01 .00 .00 .15 .03 14 6 14 12.00 .02 .00 .00 .31 .11 15 5 15 25.50 .01 .00 .00 .29 .06 16 15 16 13.50 .05 .00 .00 .34 .14 17 3 17 .00 .00 .00 .00 .00 .00 18 17 18 .00 .00 .00 .00 .00 • .00 19 18 19 .00 .00 .00 .00 .00 .00 20 19 20 .00 .00 .00 .00 .00 .00 21 12 21 -8.14 .00 .00 .00 - .05 .00 22 21 22 -8.14 .00 .00 .00 -.05 .00 23 22 23 -11.02 -.01 .00 .00 -.13 -.01 24 23 24 -35.02 -.05 .00 .00 -.40 -.11 25 22 25 -24.13 -.01 .00 .00 -.15 -.01 26 25 26 -55.63 -.03 .00 .00 -.36 -.07 27 26 24 -67.63 -.02 .00 .00 -.43 -.10 28 24 1 - 114.64 -.07 .00 .00 -.73 -.25 29 0 1 280.50 .00 .00 .00 1.79 1.33 0 ]UNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 1 .00 517.50 287.00 99.88 2 19.50 517.49 286.00 100.31 3 .00 517.42 284.00 101.15 4 36.00 517.40 283.00 101.57 5 10.50 517.38 281.00 102.43 6 10.50 517.37 282.00 101.99 7 9.00 517.37 282.00 101.99 8 1.50 517.37 282.00 101.99 9 7.50 517.37 282.00 101.99 10 12.00 517.37 286.00 100.26 11 24.00 517.38 287.00 99.83 12 .00 517.37 287.00 99.83 13 6.00 517.36 279.00 103.29 14 12.00 517.35 279.00 103.28 15 12.00 517.37 281.00 102.43 16 13.50 517.32 279.00 103.27 17 .00 517.42 284.00 101.15 18 .00 517.42 284.00 101.15 19 .00 517.42 284.00 101.1S 20 .00 517.42 282.00 102.02 21 .00 517.37 288.00 99.39 22 27.00 517.37 288.00 99.39 23 24.00 517.38 290.00 98.53 24 12.00 517.43 291.00 98.12 25 31.50 S17.38 294.00 96.80 26 12.00 517.41 297.00 95.51 THE NET SYSTEM DEMAND = 280.50 SUMMARY OF INFLOWS( +) AND OUTFLOWS( -) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE 29 280.50 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 280.50 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = .00 Page 2 1 ••"V' I V r• ._ CR76B.OUT 1 FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG A SUMMARY OF THE ORIGINAL DATA FOLLOWS 0 PIPE N0. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 1 1 2 (FEET) .0 (INCHES) 150.0 .00 2 2 3 307.0 8.0 150.0 .00 3 3 4 95.0 8.0 150.0 .00 4 4 5 280.0 8.0 150.0 .00 5 5 6 283.0 8.0 150.0 .00 6 6 7 321.0 8.0 150.0 .00 7 7 8 165.0 8.0 150.0 .00 8 8 9 34.0 8.0 150.0 .00 9 9 10 336.0 8.0 150.0 .00 10 10 11 235.0 6.0 150.0 .00 11 11 2 702.0 6.0 150.0 .00 12 10 12 129.0 8.0 150.0 .00 13 7 13 184.0 4.0 150.0 .00 14 6 14 186.0 4.0 150.0 .00 15 5 15 124.0 6.0 150.0 .00 16 15 16 356.0 4.0 150.0 .00 17 3 17 12.0 8.0 150.0 .00 18 17 18 488.0 8.0 150.0 .00 19 18 19 17.0 8.0 150.0 .00 20 19 20 517.0 8.0 150.0 .00 21 12 21 106.0 8.0 150.0 .00 22 21 22 61.0 8.0 150.0 .00 23 22 23 456.0 6.0 150.0 .00 24 23 24 469.0 6.0 150.0 .00 25 22 25 632.0 8.0 150.0 .00 26 25 26 421.0 8.0 150.0 .00 27 26 24 240.0 8.0 150.0 .00 28 24 1 270.0 8.0 150.0 .00 29 0 1 1.0 8.0 150.0 .00 + 503.60 A SUCCESSFUL GEOMETRIC VERIFICATION HAS BEEN COMPLETED ()JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES 1 .00 287.00 1 28 29 2 19.50 286.00 1 2 11 3 .00 284.00 2 3 17 4 36.00 283.00 3 4 5 10.50 281.00 4 5 15 6 10.50 282.00 5 6 14 7 9.00 282.00 6 7 13 8 1.50 282.00 7 8 9 7.50 282.00 8 9 10 12.00 286.00 9 10 12 11 24.00 287.00 10 11 12 .00 287.00 12 21 13 6.00 279.00 13 14 12.00 279.00 14 15 12.00 281.00 15 16 16 13.50 279.00 16 17 .00 284.00 17 18 18 .00 284.00 18 19 19 .00 284.00 19 20 20 .00 282.00 20 21 1000.00 288.00 21 22 22 27.00 288.00 22 23 25 23 24.00 290.00 23 24 24 1.2.00 291.00 24 27 28 25 31.50 294.00 25 26 26 12.00 297.00 26 27 OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD 0 THIS SYSTEM HAS 29 PIPES WITH 26 )UNCTIONS . 3 LOOPS AND 1 FGNS 1 THE RESULTS ARE OBTAINED AFTER 4 TRIALS WITH AN ACCURACY = .00238 OCastle Rock Phases 7 & 8 06/07/10 File CR788 )NH Proposed water system w/ FGN (94 psi, 03.6' msl) • caste Rock or. 8" wL (1417) Peak Demand of 1.5 gpm /con (187 cons) w/ 1000 gpm Fire Flow 0 FH1 (Node 21) 0 PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL /1000 1 1 2 665.63 .13 .00 .00 4.25 6.60 2 2 3 409.04 .82 .00 .00 2.61 2.68 Page 1 - --.- L.......-,.....• v• q - 1,_, ..... • CR788.0UT 3 3 4 409.04 .25 .00 .00 2.61 2.68 4 4 5 373.04 .63 .00 .00 2.38 2.26 5 5 6 337.04 .53 .00 .00 2.15 1.87 6 6 7 314.54 .53 .00 .00 2.01 1.65 7 7 8 299.54 .25 .00 .00 1.91 1.50 8 8 9 298.04 _05 .00 .00 1.90 1.49 9 9 10 290.54 .48 .00 .00 1.85 1.42 10 10 11 - 213.09 -.76 .00 .00 -2.42 -3.25 11 11 2 - 237.09 -2.78 .00 .00 -2.69 -3.96 12 10 12 491.63 .49 .00 .00 3.14 3.76 13 7 13 6.00 .01 .00 .00 .15 .03 14 6 14 12.00 .02 .00 .00 .31 .11 15 5 15 25.50 .01 _00 .00 .29 .06 16 15 16 13.50 .05 .00 .00 .34 .14 17 3 17 .00 .00 .00 .00 .00 .00 18 17 18 .00 .00 .00 .00 .00 .00 1 19 18 19 . .00 .00 .00 .00 .00 20 19 20 .00 .00 .00 .00 .00 .00 21 12 21 491.63 .40 .00 .00 3.14 3.76 22 21 22 - 508.37 -.24 .00 .00 -3.24 -4.00 23 22 23 - 191.46 -1.21 .00 .00 -2.17 -2.66 24 23 24 - 215.46 -1.55 .00 .00 -2.44 -3.31 25 22 25 - 343.91 -1.23 .00 .00 -2.19 -1.94 26 25 26 - 375.41 -.96 .00 .00 -2.40 -2.28 27 26 24 - 387.41 -.58 .00 .00 -2.47 -2.42 28 24 1 - 614.87 -1.54 .00 .00 -3.92 -5.69 29 0 1 1280.50 .02 .00 .00 8.17 22.15 0 JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 1 .00 503.58 287.00 93.85 2 19.50 503.45 286.00 94.23 3 .00 502.63 284.00 94.74 4 36.00 502.38 283.00 95.06 5 10.50 501.74 281.00 95.66 6 10.50 501.22 282.00 94.99 7 9.00 500.69 282.00 94.76 6 1.50 500.44 282.00 94.66 9 7.50 500.39 282.00 94.64 10 12.00 499.91 286.00 92.69 11 24.00 500.67 287.00 92.59 12 .00 499.43 287.00 92.05 13 6.00 500.68 279.00 96.06 14 12.00 501.19 279.00 96.28 15 12.00 501.74 281.00 95.65 16 13.50 501.69 279.00 96.50 17 .00 502.63 284.00 94.74 18 .00 502.63 284.00 94.74 19 .00 502.63 284.00 94.74 20 .00 502.63 282.00 95.61 21 1000.00 499.03 288.00 91.45 22 27.00 499.27 288.00 91.55 23 24.00 500.49 290.00 91.21 24 12.00 502.04 291.00 91.45 25 31.50 500.50 294.00 89.48 26 12.00 501.46 297.00 88.60 THE NET SYSTEM DEMAND = 1280.50 SUMMARY OF INFLOWS( +) AND OUTFLOWS( -) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE 29 1280.50 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 1280.50 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = .00 Page 2 _ _ _ - - - C . 5 • T (i p.. CT78C.OUT 1 FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG A SUMMARY OF THE ORIGINAL DATA FOLLOWS 0 PIPE NO. NODE NOS_ LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE (FEET) (INCHES) 1 1 2 19.0 8.0 150.0 .00 2 2 3 307.0 8.0 150.0 .00 3 3 4 95.0 8.0 150.0 .00 4 4 5 280.0 8.0 150.0 .00 5 5 6 283.0 8.0 150.0 .00 6 6 7 321.0 8.0 150.0 .00 7 7 8 165.0 8.0 150.0 .00 8 8 9 34.0 8.0 150.0 .00 9 9 10 336.0 8.0 150.0 .00 10 10 11 235.0 6.0 150.0 .00 11 11 2 702.0 6.0 150.0 .00 12 10 12 129.0 8.0 150.0 .00 13 7 13 184.0 4.0 150.0 .00 14 6 14 186.0 4.0 150.0 .00 15 5 15 124.0 6.0 150.0 .00 16 15 16 356.0 4.0 150.0 .00 17 3 17 12.0 8.0 150.0 .00 18 17 18 488.0 8.0 150.0 .00 19 18 19 17.0 8.0 150.0 .00 20 19 20 517.0 8.0 150.0 .00 21 12 21 106.0 B.0 150.0 .00 22 21 22 61.0 8.0 150.0 .00 23 22 23 456.0 6.0 150.0 .00 24 23 24 469.0 6.0 150.0 .00 25 22 25 632.0 8.0 150.0 .00 26 25 26 421.0 8.0 150.0 .00 27 26 24 240.0 8.0 150.0 .00 28 24 1 270.0 B.0 150.0 .00 29 0 1 1.0 8.0 150.0 .00 + 503.60 A SUCCESSFUL GEOMETRIC VERIFICATION HAS BEEN COMPLETED 03UNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES 1 .00 287.00 1 28 29 2 19.50 286.00 1 2 11 3 .00 284.00 2 3 17 4 36.00 283.00 3 4 5 10.50 281.00 4 5 15 6 10.50 282.00 5 6 14 7 9.00 282.00 6 7 13 8 1.50 282.00 7 8 9 7.50 282.00 8 9 10 12.00 286.00 9 10 12 11 24.00 287.00 10 11 12 .00 287.00 12 21 13 6.00 279.00 13 14 12.00 279.00 14 15 12.00 281.00 15 16 16 13.50 279.00 16 17 .00 284.00 17 18 18 .00 284.00 18 19 19 .00 284.00 19 20 20 .00 282.00 20 21 .00 288.00 21 22 22 27.00 288.00 22 23 25 23 24.00 290.00 23 24 24 12.00 291.00 24 27 28 25 1031.50 294.00 25 26 26 12.00 297.00 26 27 OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD 0 THIS SYSTEM HAS 29 PIPES WITH 26 JUNCTIONS , 3 LOOPS AND 1 FGNS 1 THE RESULTS ARE OBTAINED AFTER 4 TRIALS WITH AN ACCURACY = .00138 ()Castle Rock Phases 7 & 6 06 /OT /10 File CR78C )NH Proposed water system w/ FGN (94 psi. 503.6' msl) 0 Caste Rock Dr. 8" MIL (FH7) Peak Demand of 1.S gpm /con (187 cons) w/ 1000 gpm Fire Flow 0 FH2 (Node 25) 0 PIPE NO. NOOE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL /1000 1 1 2 556.03 .09 .00 .00 3.55 4.73 2 2 3 343.28 .59 .00 .00 2.19 1.93 Page 1 � . / 1\, v, , 1 g---- r. • CT78C.DUT 3 3 4 343.28 .18 .00 .00 2.19 1.93 4 4 5 307.28 .44 .00 .00 1.96 1.58 5 5 6 271.28 .35 .00 .00 1.73 1.25 6 6 7 248.78 .34 .00 .00 1.59 1.07 7 7 8 233.78 .16 .00 .00 1.49 .95 8 8 9 232.28 .03 .00 .00 1.48 .94 9 9 10 224.78 .30 .00 .00 1.43 .88 10 10 11 - 169.25 -.50 .00 .00 -1.92 -2.12 11 11 2 - 193.25 -1.90 .00 .00 - 2.19 - 2.71 12 10 12 382.03 .30 .00 .00 2.44 2.36 13 7 13 6.00 .01 .00 .00 .15 .03 14 6 14 12.00 .02 .00 .00 .31 .11 15 5 15 25.50 .01 .00 .00 .29 .06 16 15 16 13.50 .05 .00 .00 .34 .14 17 3 17 .00 .00 .00 .00 .00 .00 18 17 18 .00 .00 .00 .00 .00 .00 19 18 19 .00 .00 .00 .00 .00 .00 20 19 20 .00 .00 .00 .00 .00 .00 21 12 21 382.03 .Z5 .00 .00 2.44 2.36 22 21 22 382.03 .14 .00 23 22 23 - 111.53 -.45 .00 .00 -1.27 -.98 24 23 24 - 135.53 -.66 .00 .00 -1.54 -1.40 25 22 25 466.56 2.16 .00 .00 2.98 3.42 I 26 25 26 - 564.94 -2.05 .00 .00 -3.61 -4.87 27 26 24 - 576.94 -1.21 .00 .00 -3.68 -5.06 28 24 1 - 724.47 -2.08 .00 .00 -4.62 -7.72 29 0 1 1280.50 .02 .00 .00 8.17 22.15 0 JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 1 .00 503.58 287.00 93.85 2 19.50 503.49 286.00 94.24 3 .00 502.89 284.00 94.85 4 36.00 502.71 283.00 95.21 5 10.50 502.27 281.00 95.88 6 10.50 501.91 282.00 95.30 7 9.00 501.57 282.00 95.15 8 1.50 501.42 282.00 95.08 9 7.50 501.38 282.00 95.07 10 12.00 S01.09 286.00 93.20 11 24.00 501.59 287.00 92.99 12 .00 500.78 287.00 92.64 13 6.00 501.57 279.00 96.45 14 12.00 501.89 279.00 96.59 15 12.00 502.26 281.00 95.88 16 13.50 502.21 279.00 96.72 17 8 . 50 284.00 94.85 19 .00 502.89 284.00 94.85 20 .00 502.89 282.00 95.72 21 .00 500.53 288.00 92.10 22 27.00 500.39 288.00 92.04 23 24.00 500.84 290.00 91.36 24 12.00 501.49 291.00 91.21 25 1031.50 498.23 294.00 88.50 26 12.00 500.28 297.00 88.09 THE NET SYSTEM DEMAND = 1280.50 SUMMARY OF INFLOWS(+) AND OUTFLOWS( -) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE 29 1280.50 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES - 1280.50 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES - .00 Page 2 CR78D.OUT 1 FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG A SUMMARY OF THE ORIGINAL DATA FOLLOWS 0 PIPE N0. NODE N05. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 1 1 2 (FEET) (INCHES) 150.0 .00 2 2 3 307.0 8.0 150.0 .00 3 3 4 95.0 8.0 150.0 .00 4 4 5 280.0 8.0 150.0 .00 5 5 6 283.0 8.0 150.0 .00 6 6 7 321.0 8.0 150.0 .00 7 7 8 165.0 8.0 150.0 .00 8 8 9 34.0 8.0 150.0 .00 9 9 10 336.0 8.0 150.0 .00 10 10 11 235.0 6.0 150.0 .00 11 11 2 702.0 6.0 150.0 .00 12 10 12 129.0 8.0 150.0 .00 13 7 13 184.0 4.0 150.0 .00 14 6 14 186.0 4.0 150.0 .00 15 5 15 124.0 6.0 150.0 .00 16 15 16 356.0 4.0 150.0 .00 17 3 17 12.0 8.0 150.0 .00 18 17 18 488.0 8.0 150.0 .00 19 18 19 17.0 8.0 150.0 .00 20 19 20 517.0 8.0 150.0 .00 21 12 21 106.0 8.0 150.0 .00 22 21 22 61.0 8.0 150.0 .00 23 22 23 456.0 6.0 150.0 .00 24 23 24 469.0 6.0 150.0 .00 25 22 25 632.0 8.0 150.0 .00 26 25 26 421.0 8.0 150.0 .00 27 26 24 240.0 8.0 150.0 .00 28 24 1 270.0 8.0 150.0 .00 29 0 1 1.0 8.0 150.0 .00 + 503.60 A SUCCESSFUL GEOMETRIC VERIFICATION HAS BEEN COMPLETED °JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES 1 .00 287.00 1 28 29 2 19.50 286.00 1 2 11 3 .00 284.00 2 3 17 4 36.00 283.00 3 4 5 10.50 281.00 4 5 15 6 10.50 282.00 5 6 14 7 9.00 282.00 6 7 13 8 1.50 282.00 7 8 9 7.50 282.00 8 9 10 12.00 286.00 9 10 12 11 24.00 287.00 10 11 12 .00 287.00 12 21 13 6.00 279.00 13 14 12.00 279.00 14 15 12.00 281.00 15 16 16 13.50 279.00 16 17 .00 284.00 17 18 18 .00 284.00 18 19 19 .00 284.00 19 20 20 .00 282.00 20 21 .00 288.00 21 22 22 27.00 288.00 22 23 25 23 1024.00 290.00 23 24 24 12.00 291.00 24 27 28 25 31.50 294.00 25 26 26 12.00 297.00 26 27 OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD 0 THIS SYSTEM HAS 29 PIPES WITH 26 )UNCTIONS , 3 LOOPS AND 1 FGNS 1 THE RESULTS ARE OBTAINED AFTER 4 TRIALS WITH AN ACCURACY - .00231 OCastle Rock Phases 7 8 S 06/07/10 File CR78D JNH Proposed Water System vi/ FGN (94 psi 503.6' msl) 11 castle Rock or. 8" wL (FH7) Peak Demand of 1.5 gpm /con (1 87 cons) w/ 1000 gpm Fire Flow p FH3 (Node 23) 0 PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL /1000 1 1 2 538.43 .08 .00 .00 3.44 4.45 2 2 3 332.71 .56 .00 .00 2.12 1.63 Page 1 CR780.OUT 3 3 4 332.71 .17 .00 .00 2.12 1.83 4 4 5 296.71 .41 .00 .00 1.89 1.48 5 5 6 260.71 .33 .00 .00 1.66 1.16 6 6 7 238.21 .32 .00 .00 1.52 .98 7 7 8 223.21 .14 .00 .00 1.42 .87 8 8 9 221.71 .03 .00 .00 1.42 .86 9 9 10 214.21 .27 .00 .00 1.37 .81 10 10 11 - 162.22 -.46 .00 .00 -1.84 -1.96 11 11 2 - 186.22 -1.78 .00 .00 -2.11 -2.53 12 10 12 364.43 .28 .00 .00 2.33 2.16 13 7 13 6.00 .01 .00 .00 .15 .03 14 6 14 12.00 .02 .00 .00 .31 .11 15 5 15 25.50 .01 .00 .00 .29 .06 16 15 16 13.50 .05 .00 .00 .34 .14 17 3 17 .00 .00 .00 .00 .00 .00 18 17 18 .00 .00 .00 .00 .00 .00 19 18 19 .00 .00 .00 .00 .00 .00 20 19 20 .00 .00 .00 .00 .00 .00 21 12 21 364.43 .23 .00 .00 2.33 2.16 22 21 22 364.43 .13 .00 .00 2.33 2.16 23 22 23 501.67 7.23 .00 .00 5.69 15.86 24 23 24 - 522.33 -8.01 .00 .00 -5.93 -17.09 25 22 25 - 164.24 -.31 .00 .00 -1.05 -.49 26 25 26 - 195.74 -.29 .00 .00 -1.25 -.68 27 26 24 - 207.74 -.18 .00 .00 -1.33 -.76 28 24 1 - 742.07 -2.18 .00 .00 -4.74 -8.07 29 0 1 1280.50 .02 .00 .00 8.17 22.15 0 7UNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 1 .00 503.58 287.00 93.85 2 19.50 503.49 286.00 94.2S 3 .00 502.93 284.00 94.87 4 36.00 502.76 283.00 95.23 5 10.50 502.35 281.00 95.92 6 10.50 502.02 282.00 95.34 7 9.00 501.70 282.00 95.20 8 1.50 501.56 282.00 95.14 9 7.50 501.53 282.00 95.13 10 12.00 501.26 286.00 93.28 11 24.00 501.72 287.00 93.04 12 .00 500.98 287.00 92.72 13 6.00 501.70 279.00 96.50 14 12.00 502.00 279.00 96.63 15 12.00 502.34 281.00 95.91 16 13.50 502.29 279.00 96.76 17 .00 502.93 284.00 94.87 18 .00 502.93 284.00 94.87 19 .00 502.93 284.00 94.87 20 .00 502.93 282.00 95.74 21 .00 500.75 288.00 92.19 22 27.00 500.62 288.00 92.13 23 1024.00 493.39 290.00 88.13 24 12.00 501.40• 291.00 91.17 25 31.50 500.93 294.00 89.67 26 12.00 501.22 297.00 88.49 THE NET SYSTEM DEMAND = 1280.50 SUMMARY OF INFLOWS( +) AND OUTFLOWS( -) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE 29 1280.50 • THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 1280.50 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES Page 2