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As shown in the figure, water flows through the horizontal branching pipe at a rate 280 L/s. Viscous effects are negligible. 13. Determine the water speed at section 2. A. 7.54 m/s D. 9.36 m/s 14. Determine the pressure at section 3. A. 50.24 kPa 15. Determine the flow rate at section 4. B. 8.12 m/s C. 8.82 m/s B. 55.92 kPa C. 45.68 kPa D. 47.52 kPa A. 109.7 L/s B. 98.3 L/s C. 132.1 L/s D. 85.2 LS

As shown in the figure, water flows through the horizontal branching pipe at a rate 280 L/s. Viscous effects are negligible. 13. Determine the water speed at section 2. A. 7.54 m/s D. 9.36 m/s 14. Determine the pressure at section 3. A. 50.24 kPa 15. Determine the flow rate at section 4. B. 8.12 m/s C. 8.82 m/s B. 55.92 kPa C. 45.68 kPa D. 47.52 kPa A. 109.7 L/s B. 98.3 L/s C. 132.1 L/s D. 85.2 LS

Structural Analysis
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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12. The weir is a Cipolletti with L = 4.3 m. A. 9.67% B. 13.28% C. 10.24% D. 15.32% Situation 5: As shown in the figure, water flows through the horizontal branching pipe at a rate 280 L/s. Viscous effects are negligible. 13. Determine the water speed at section 2. A. 7.54 m/s D. 9.36 m/s B. 8.12 m/s C. 8.82 m/s 14. Determine the pressure at section 3. A. 50.24 kPa B. 55.92 kPa C. 45.68 kPa D. 47.52 kPa 15. Determine the flow rate at section 4. A. 109.7 L/s B. 98.3 L/s C. 132.1 L/s D. 85.2 LS A= 0.007 m2 p= 35 kPa A= 0.02 m2 v = 6 m/s A= 0.1 m2 Q = 280 L/s p= 70 kPa
Transcribed Image Text:12. The weir is a Cipolletti with L = 4.3 m. A. 9.67% B. 13.28% C. 10.24% D. 15.32% Situation 5: As shown in the figure, water flows through the horizontal branching pipe at a rate 280 L/s. Viscous effects are negligible. 13. Determine the water speed at section 2. A. 7.54 m/s D. 9.36 m/s B. 8.12 m/s C. 8.82 m/s 14. Determine the pressure at section 3. A. 50.24 kPa B. 55.92 kPa C. 45.68 kPa D. 47.52 kPa 15. Determine the flow rate at section 4. A. 109.7 L/s B. 98.3 L/s C. 132.1 L/s D. 85.2 LS A= 0.007 m2 p= 35 kPa A= 0.02 m2 v = 6 m/s A= 0.1 m2 Q = 280 L/s p= 70 kPa
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