situation XIX: The head loss in74 m of 150 mm diametter pipe is kown to be 9 m when oil (s0.90) flows at 0.057 m^3/s. Assume viscosity of oil is 0.0389 Pa.s.49.Determine the Reynolds NumberTa. 11 210b. 13 17015 140d. 19 830C.50. Determine the friction factor.a. 0.019b. 0.034C.0.044d. 0.07851.Find the shear stress at the wall pipe:a. 39.91 N/m2b. 48.19 N/m2c. 56.23 N/m2d. 60.18 N/m"Situation XX: In the figure shown,m. length of pipe fromn the reservoir to the pump is 120n to then in the pozle is 1000 m. The diameters of pipes are 0.60 and 0.45 m respectively.inor Jossesa reserv7 m dow c. 56.23 N/m3d. 60.18 N/m2Situatton XC: In the figure shown, z,-4 m, length of pipe from the reservoir to the pump is 120m, from the pump to the nozzle is 1000 m. The diameters of pipes are 0.60 and 0.45 m respectively.The gage pressure at B (the suction side of the pump) is -64 KPa. Neglect minor losses.D.B.0.45 m diam.LcD=1000 mf%=0.02%3DZp = 4 m0.60 m diam.LAB= 120 mf%30.0252. Compute the velocity of water in pipe AB.a. 2.297 m/sb. 1.452 m/sc. 3.147 m/sd. 2.672 m/s53. Compute the velocity of water in pipe CD.a. 1.23 m/sb. 4.08 m/sC. 3.56 m/sd. 5.59 m/s54. Compute the discharge of the pipe from A to B due to pumping.a. 0.65 m/sb. 0.45 m2/sc. 0.89 m/sd. 0.25 m /s60m. -0.02 m and loss of head

Given that: Length of pipe, L=74mDiameter of pipe, d=150 mmHead loss,…

situation XIX: The head loss in 74 m of 150 mm dianeter pipe is known to be 9 m when oil (s 0.90) flows at 0.057 m^3/s. Assume viscosity of oil is 0.0389 Pa.s. 49.Determine the Reynolds Number. a. 11 210

situation XIX: The head loss in 74 m of 150 mm dianeter pipe is known to be 9 m when oil (s 0.90) flows at 0.057 m^3/s. Assume viscosity of oil is 0.0389 Pa.s. 49.Determine the Reynolds Number. a. 11 210

Structural Analysis

6th Edition

ISBN:9781337630931

Author:KASSIMALI, Aslam.

Publisher:KASSIMALI, Aslam.

Chapter2: Loads On Structures

Section: Chapter Questions

Problem 1P

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Situation XX: In the figure shown, z, = 4 m, length of pipe from the reservoir to the pump is 120 %3D m, from the pump to the nozzle is 1000 m. The diameters of pipes are 0.60 and 0.45 m respectively. The gage pressure at B (the suction side of the pump) is -64 KPa. Neglect minor losses. В C P. 0.45 m diam. LCD = 1000 m %3D Zp = 4 m f = 0.02 0.60 m diam. LAB = 120 m f = 0.02 %3D 52. Compute the velocity of water in pipe AB. a. 2.297 m/s b. 1.452 m/s c. 3.147 m/s d. 2.672 m/s 53. Compute the velocity of water in pipe CD. a. 1.23 m/s b. 4.08 m/s c. 3.56 m/s d. 5.59 m/s 54. Compute the discharge of the pipe from A to B due to pumping. a. 0.65 m3/s b. 0.45 m3/s c. 0.89 m³/s d. 0.25 m3/s 60 m, f= 0.02 m and loss of head ith
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-8.33 -0.12 8.33 (1) 0.12 -L Darcy Experiment A set-up of Darcy Experiment involves measuring the pressure head at two piezometers separated a distance, L. Given the set-up shown, determine the hydraulic gradient if the hydraulic head at (1) is 66 cm, hydraulic head at (2) is 54 cm, and the travel distance is 100 cm. h (2) e - - - -