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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
Structural Analysis
6th Edition
ISBN:9781337630931
Author:KASSIMALI, Aslam.
Publisher:KASSIMALI, Aslam.
Chapter2: Loads On Structures
Section: Chapter Questions
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situation XIX: The head loss in74 m of 150 mm diametter pipe is kown 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 NumberT a. 11 210 b. 13 170 15 140 d. 19 830 C. 50. Determine the friction factor. a. 0.019 b. 0.034 C. 0.044 d. 0.078 51.Find the shear stress at the wall pipe: a. 39.91 N/m2 b. 48.19 N/m2 c. 56.23 N/m2 d. 60.18 N/m" Situation XX: In the figure shown, m. length of pipe fromn the reservoir to the pump is 120 n to the n in the pozle is 1000 m. The diameters of pipes are 0.60 and 0.45 m respectively. inor Josses a reserv 7 m dow
Transcribed Image Text:situation XIX: The head loss in74 m of 150 mm diametter pipe is kown 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 NumberT a. 11 210 b. 13 170 15 140 d. 19 830 C. 50. Determine the friction factor. a. 0.019 b. 0.034 C. 0.044 d. 0.078 51.Find the shear stress at the wall pipe: a. 39.91 N/m2 b. 48.19 N/m2 c. 56.23 N/m2 d. 60.18 N/m" Situation XX: In the figure shown, m. length of pipe fromn the reservoir to the pump is 120 n to the n in the pozle is 1000 m. The diameters of pipes are 0.60 and 0.45 m respectively. inor Josses a reserv 7 m dow
c. 56.23 N/m3 d. 60.18 N/m2 Situatton XC: In the figure shown, z,-4 m, length of pipe from the reservoir to the pump is 120 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. D. B. 0.45 m diam. LcD=1000 m f%=0.02 %3D Zp = 4 m 0.60 m diam. LAB= 120 m f%30.02 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 m/s b. 0.45 m2/s c. 0.89 m/s d. 0.25 m /s 60m. -0.02 m and loss of head
Transcribed Image Text:c. 56.23 N/m3 d. 60.18 N/m2 Situatton XC: In the figure shown, z,-4 m, length of pipe from the reservoir to the pump is 120 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. D. B. 0.45 m diam. LcD=1000 m f%=0.02 %3D Zp = 4 m 0.60 m diam. LAB= 120 m f%30.02 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 m/s b. 0.45 m2/s c. 0.89 m/s d. 0.25 m /s 60m. -0.02 m and loss of head
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