R 44 A-PA 1'-712g some to F# u=vy vr Flow 4. Consider flow of a liquid...
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R 44 A-PA 1'-7₁12g some to F# u=vy vr Flow 4. Consider flow of a liquid (p = 10 kg/m³; p = 0.01 N.s/m²) through a pipe of circular cross section of radius R-1 m. A pitot tube with a manometer is connected to the pipe as shown. One end of the manometer is connected to the pipe wall, the other end is located along the centerline of the pipe. The manometer fluid has a density of 5000 Kg/m³, and the reading of the manometer is as shown below to mm). Find the pressure difference between two locations A and B in the pipe that are 2 m apart as shown. Vr-Ve Ostagnat pt Vr (1²) ag PITUT TUBE Tromm min A Manometes PIPE B3 C R 44 A-PA 1'-7₁12g some to F# u=vy vr Flow 4. Consider flow of a liquid (p = 10 kg/m³; p = 0.01 N.s/m²) through a pipe of circular cross section of radius R-1 m. A pitot tube with a manometer is connected to the pipe as shown. One end of the manometer is connected to the pipe wall, the other end is located along the centerline of the pipe. The manometer fluid has a density of 5000 Kg/m³, and the reading of the manometer is as shown below to mm). Find the pressure difference between two locations A and B in the pipe that are 2 m apart as shown. Vr-Ve Ostagnat pt Vr (1²) ag PITUT TUBE Tromm min A Manometes PIPE B3 C
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Related Book For
Fundamentals Of Momentum Heat And Mass Transfer
ISBN: 9781118947463
6th Edition
Authors: James Welty, Gregory L. Rorrer, David G. Foster
Posted Date:
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