Calculate the pipe diameters, discharges by Dead End Method Elevation of the reservoir bottom, zreservoir = 80 m height of water in the reservoir, hf = 6 m Transmission discharge, Qtransmission = 70 l/s Population, Ng = 3813

Calculate the pipe diameters, discharges by Dead End Method Elevation of the reservoir bottom, zreservoir = 80 m height of water in the reservoir, hf = 6 m Transmission discharge, Qtransmission = 701/s Population, Ng = 38131 k Pipe No 0 1 2 Joint No 0 1 2 2 2 2 1 4 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 Joint 0-1 1-12 12-13 13 - 16 12-14 1-5 5-14 5.9 9-15 15 - 16 14-15 15 - 18 16-17 1-2 2-3 2 - 6 3-7 5-6 6.7 7. 10 9-10 L (m) 56 62 63 125 48 86 47 74 44 41 77 47 37 50 49 70 56 39 48 45 82 33 49 36 2 1 2 2 2 1 1 1 2 2 1 2 1 1 2 2 1 1 1 5 6 7 8 9 10 11 12 13 14 15 16 17 18 Elev. (m) 80.0 50.0 46.5 43.2 40.0 28.8 29.2 29.6 25.8 18.0 20.0 15.6 35.6 30.0 27.0 16.8 14.0 10.0 10.0 7-8 10-11 Pipe friction coefficient for Hazen - Williams Equation (C = 95) Hazen - Williams Equation: 0,299 C D 3.63 (30.01 (80.0) 150.07 (35.6) 12 80 127.0) 14 146 17 70 28.8) (10,0) 60 16 (14.0) (43.27 50 15 (29.21 (168) (29.6) (40.0) (18.01 18 (10,0) 10 (20.0) 30 (25.8) 20 10 11 (15.6) 10 2/6 (30.01 (80.0) (50.0) (35.6) 80 127.01 17 (46.5) (10,0) 70 28.8) 16 (14.0) 60 (43.21 15 2116.8) 50 (40.0) (29.6) (18.01 18 (10.01 40 (20.01 10 (25.8) 30 20 11 (15.6) 10 Calculate the pipe diameters, discharges by Dead End Method Elevation of the reservoir bottom, zreservoir = 80 m height of water in the reservoir, hf = 6 m Transmission discharge, Qtransmission = 701/s Population, Ng = 38131 k Pipe No 0 1 2 Joint No 0 1 2 2 2 2 1 4 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 Joint 0-1 1-12 12-13 13 - 16 12-14 1-5 5-14 5.9 9-15 15 - 16 14-15 15 - 18 16-17 1-2 2-3 2 - 6 3-7 5-6 6.7 7. 10 9-10 L (m) 56 62 63 125 48 86 47 74 44 41 77 47 37 50 49 70 56 39 48 45 82 33 49 36 2 1 2 2 2 1 1 1 2 2 1 2 1 1 2 2 1 1 1 5 6 7 8 9 10 11 12 13 14 15 16 17 18 Elev. (m) 80.0 50.0 46.5 43.2 40.0 28.8 29.2 29.6 25.8 18.0 20.0 15.6 35.6 30.0 27.0 16.8 14.0 10.0 10.0 7-8 10-11 Pipe friction coefficient for Hazen - Williams Equation (C = 95) Hazen - Williams Equation: 0,299 C D 3.63 (30.01 (80.0) 150.07 (35.6) 12 80 127.0) 14 146 17 70 28.8) (10,0) 60 16 (14.0) (43.27 50 15 (29.21 (168) (29.6) (40.0) (18.01 18 (10,0) 10 (20.0) 30 (25.8) 20 10 11 (15.6) 10 2/6 (30.01 (80.0) (50.0) (35.6) 80 127.01 17 (46.5) (10,0) 70 28.8) 16 (14.0) 60 (43.21 15 2116.8) 50 (40.0) (29.6) (18.01 18 (10.01 40 (20.01 10 (25.8) 30 20 11 (15.6) 10