network manually by constructing and solving a system of equations. Check your manual answers by constructing a computer model of the system and then performing a computer simulation of the model. You should use the EPANET computer program. P2 Does this system operate properly? If it does not, suggest changes so that the system operates at an acceptable level of service? A R-1 P13 CEE 333 HW #1 Not To Scale N B P4 Pump P3 C Water Resources Engineering Due: 1/31/2024 P1 D P6 IP7 P12 K P15 M P5 Figure 1 H P19 S P8 E . P18 P9 P16 P14 R P11 P P17 P10 Not To Scale F G Q Pipe 1 2 3 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 Begin Node R-1 D D | J J G G | K K J P O H End Node I A C B E D J H G F O K N L M P Q R S Table 1 Pipe Data Length (Ft) 500 2300 1200 600 1000 2500 2750 3200 1700 770 1500 1250 850 1500 250 2750 450 750 450 Diameter (In) 16 6 6 6 8 8 8 8 6 6 8 4 6 8 8 6 4 8 4 C-Factor 110 120 120 110 110 90 120 100 110 125 110 120 110 115 100 110 100 120 120 Minor Loss (K₁) 10 0 0 0 0 3 0 0 10 0 0 5 0 0 0 7.5 3 0 0 Node R-1 A B C D F G H I Elevation (msl) 1380 1400 1425 1450 1430 1420 1450 1460 1440 1485 Table 2 - Node Data Demand (Gpm) N/A 0 500 120 300 150 20 0 220 75 Node Pump Discharge (Gpm) 0 3,600 7,500 J K L M N O P Q S Table 3-Pump Data Pump Head (Ft) 350 335 285 Elevation (msl) 1430 1425 1420 1450 1420 1460 1500 1520 1495 1445 Demand (Gpm) 100 335 150 100 50 75 25 100 50 350 1. Is the system shown in Figure 2 balanced using the flows provided in Table 4? Note the flow directions given. Describe why the flows are correct or why are they incorrect? Provide numerical evidence to support your claim. P2 A R-1 P13 P20 B P4 Pump P3 C P1 D M P6 I P7 P12 K P15 P5 P23 Figure 2 HP19 S P8 E P21 P18 P9 P16 P14 R P11 P17 P22 P10 R-2 G Not To Scale Q Pipe 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 Begin Node R-1 B B D | J J G G 1 K K J P O H A E L L End Node | A C B E D J H G F O K N L M P Q R S C Q M Table 4- Pipe Data Length (Ft) 500 2300 1200 600 1000 2500 2750 3200 1700 770 1500 1250 850 1500 250 2750 450 750 450 1350 300 3560 850 Diameter (In) 16 6 6 6 ∞ ∞ 8 6 6 8 4 6 ∞ ∞ 8 6 8 4 6 8 6 6 C-Factor 110 120 120 110 110 90 120 100 110 125 110 120 110 115 100 110 100 120 120 120 110 120 120 Minor Loss (K₁) 10 0 0 0 0 3 0 0 10 0 0 5 0 0 0 7.5 3 0 0 0 0 0 0 Flow (Gpm) 3000 40 80 620 70 850 1655 570 645 300 345 420 50 15 50 340 315 270 350 40 220 215 50