1. Lab 6: Energy Losses in Pipe Bends: (20pt) (Please show work) Type of fitting Manometer Manometer reading h1 reading h2 (mm) Head loss (h1 V² (mm) -h2) (mm) Volume Time Flowrate Velocity (L) (s) Q (m^3/s) (m/s) 2g K Re Bend 220 216 5 25 D= 0.022m, kinematic viscosity, v = 1.002 * 10 m²/s, g = 9.81 m/s². Calculate: V-/2g, K and Re

Structural Analysis
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Author:KASSIMALI, Aslam.
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1. Lab 6: Energy Losses in Pipe Bends: (20pt) (Please show work)
Type of
fitting
Manometer Manometer
reading h1 reading h2
(mm)
Head
loss (h1
V²
(mm)
-h2)
(mm)
Volume Time Flowrate Velocity
(L) (s) Q (m^3/s) (m/s)
2g
K
Re
Bend
220
216
5
25
D= 0.022m, kinematic viscosity, v = 1.002 * 10 m²/s, g = 9.81 m/s². Calculate: V-/2g, K and Re
Transcribed Image Text:1. Lab 6: Energy Losses in Pipe Bends: (20pt) (Please show work) Type of fitting Manometer Manometer reading h1 reading h2 (mm) Head loss (h1 V² (mm) -h2) (mm) Volume Time Flowrate Velocity (L) (s) Q (m^3/s) (m/s) 2g K Re Bend 220 216 5 25 D= 0.022m, kinematic viscosity, v = 1.002 * 10 m²/s, g = 9.81 m/s². Calculate: V-/2g, K and Re
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