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                                                   Water Hydraulics, Transmission, and Appurtenances
                                          Chapter 5
                                                                                                                            2
                                                                                       the pressure is 35 psig (242.9 kPa = 242.9 kN/m ). At point B
                                                                                       5,000 ft (1,524 m) downstream of the pipe, the elevation is 135 ft
                                                                                                                                     2
                                                                                       (41.148 m) and the pressure is 40 psig (277.6 kPa = 277.6 kN/m ).
                                                                                       Determine the head loss between points A and B.
                                                                                            A 24 in. (609.6 mm), 5,000 ft (1524 m) pipeline carries
                                                                                       5.48
                                                  H A
                                                                                                   3
                                                                                       1.6 ft /s (0.453 m /s) of water between points A and B. The head
                                                                                       loss between A and B is 8.46 ft (2.56 m). Determine the velocity of
                                                                                       flow and the pipe friction factor f.
                                                                                       5.49
                                                                                            A water jet shown in Fig. 5.51 flows vertically upward from
                                                       A
                                                                                       a nozzle with a vertical velocity of 16 ft/s (4.8768 m/s) and a flow
                                                                                                3
                                                                                                             3
                                                                                       rate of 0.03 ft /s (0.0008496 m /s). Above the nozzle at a distance
                                    Figure 5.49 Standard pitot tube.  B  H B           5.47  3  At point A in a pipeline, the elevation is 155 ft (47.244 m);
                                                                                       h = 6 in. (152.4 mm), there is a horizontal plate weighing 0.5 lb
                                                                                       (0.227 kg). Determine the reaction force F which is required to hold
                                    5.42  Determine the flow from a standard orifice J shown in Fig.  the plate stationary.
                                    5.48. The head above the orifice H = 20 ft (6.096 m), the orifice
                                    diameter equals 4.5 in. (114.3 mm), and discharge coefficient C =   Reaction force
                                                                                  d
                                    0.594.                                                                   F
                                                                                               Horizontal plate
                                    5.43  The pitot tube shown in Fig. 5.49 has a coefficient of 0.9850.
                                    It is used to measure the velocity of water at the center of a pipe.
                                    Assume a stagnation pressure head H of 19 ft (5.7912 m) and the
                                                               B
                                    static pressure head H in the pipe of 16 ft (4.8768 m). Determine                        h
                                                    A
                                    the velocity at A and the pressure at B.
                                    5.44  Given an over-simplified Moody diagram (Fig. 5.50) and        V, Q   Nozzle
                                    the original Moody diagram (Fig. 5.11), explain the applications of
                                    curves A, B, C, D, and E.
                                                                                                         Center line
                                                                                       Figure 5.51 Water jet from a nozzle.
                                                                            E
                                                                                       5.50  A rectangular wood block floats in water with 6.2 in. (157.48
                                                                            D          mm) projecting above the water surface. If the same wood block
                                           f
                                                                                       is placed in an organic solvent of specific gravity 0.81, the wood
                                                                            C          block projects 4.2 in. (106.68 mm) above the surface of the organic
                                                  A                                    solvent. Determine the specific gravity of the wood block.
                                                                            B
                                                 2,000     R
                                                                                       REFERENCES
                                    Figure 5.50 Simplified Moody diagram.
                                                                                       Al-Dhowalia, K. and Shammas, N. K., Leak detection and quan-
                                                                                          tification of losses in a water network, International Journal
                                    5.45  Briefly and precisely define                    of Water Resources Development, vol. 7, no. 1, pp. 30–38,
                                      1. The Moody diagram                                1991.
                                      2. The Bernoulli equation                        Bradley, J. N. and Thompson, L. R., Friction factors for large con-
                                                                                          duits flowing full, Bureau of Reclamation Engineering Mono-
                                      3. The Darcy–Weisbach formula
                                                                                          graph 7, Denver, CO, 1951.
                                      4. The Chezy formula
                                                                                       Colebrook, C. F., Turbulent flow in pipes, with particular ref-
                                      5. Hazen–Williams formula                           erence to the transition region between the smooth and
                                      6. Manning equation                                 rough pipe laws, Journal of the ICE, vol. 11, pp. 133–156,
                                    5.46  Briefly and precisely define                    1939.
                                      1. Pitot tube                                    Colebrook, C. F. and White, C. M., The reduction of carrying capac-
                                                                                          ity of pipes with age, Journal of the ICE, vol. 7, pp. 99–118,
                                      2. Stagnation pressure
                                                                                          1937–1938.
                                      3. Hydraulic gradient
                                                                                       Fair, G. M., Geyer, J. C., and Okun, D. A., Water and Wastewater
                                      4. Energy gradient                                  Engineering, vol. 1: Water Supply and Wastewater Removal,
                                      5. Friction head loss                               John Wiley & Sons, Inc., New York, 1966.
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