Q4) Water (y 9810 N/m3) flows steadily with negligible viscous effects through a pipe as shown...
Question 2 4 pts Question 1lb) If viscous effects are negligible, determine the flow rate Qt (m3/s) at Point 1 in the large pipe if h-5.8 m and V2 66m/s The density of water is 1000 kg/m3. Atmospheric pressure Patm 101.325 kPa. Gravitational acceleration g- 9.81 m/s Your answer should be in m3/s and accurate to4d.р. Question 3 3 pts If viscous effects are negligible, determine the gauge pressure p1 (kPa) at Point 1 in the large pipe for Q1...
Q.9 Water flows through the branching pipe shown in Fig. If viscous effects are negligible, determine the pres- sure at section (2) and the pressure at section (3). Az = 0.035 m 22 = 10 m Q = 1 m/s A = 0.1 m P = 300 kPa 21 = 0 V, = 14 m/s Az = 0.03 m2 2 = 0 FIGURE
Please show detailed work and write clearly. Thank you.
Q2) Water flows steadily with negligible viscous effects through a pipe as shown in the figure below. If the pipe cross section area is 0.2 m2 and the difference in manometers level (h)-7 cm (0.07 m), find the flow rate in the pipe.
Water flows steadily from the large open tank shown in the
figure below. If viscous effects are negligible, determine (a) the
flowrate, Q, (b) the mercury manometer reading, h.
4. 1m 1.9m 0.07m Mercury 0.09m
Water (p = 1,000 kg/m?) flows steadily through a 90° elbow and exits as a free jet through a nozzle, as shown below. The measured upstream gage pressure is 800 kPa. Neglect body forces and viscous effects, and disregard the height of the elbow/nozzle combination. The water velocity at any cross section is assumed to be uniform. However, the water velocity inside the elbow is not negligible compared to that in the nozzle. Consider the following: Determine the velocities V,...
A liquid of density 1230 kg/m3 flows steadily through a pipe of varying diameter and height. At Location 1 along the pipe, the flow speed is 9.31 m/s and the pipe diameter d1 is 12.9 cm . At Location 2, the pipe diameter d2 is 17.7 cm . At Location 1, the pipe is Δ y = 8.09 m higher than it is at Location 2. Ignoring viscosity, calculate the difference Δ P between the fluid pressure at Location 2...
Water flows through a pipe shaped as shown here. The pressure at the lower end of the pipe is 296 kPa and the fluid velocity is 5.00 m/s. The upper end of the pipe is 0.600 m higher and the cross-sectional area is 1/3 of the area at the lower end. Calculate the velocity at the upper end of the pipe. 15 m/s Calculate the pressure at the upper end of the pipe.
A liquid of density 1.39 × 103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.67 m/s and the pipe diameter is 11.5 cm. At location 2 the pipe diameter is 14.9 cm. At location 1 the pipe is 8.31 m higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location 1.
A liquid of density 1.11 × 103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.09 m/s and the pipe diameter is 10.9 cm. At location 2 the pipe diameter is 14.1 cm. At location 1 the pipe is 8.03 m higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location 1.
Q4 (20 pts): Water flows steadily through the funnel shown in the figure below. Throughout most of the funnel the flow is approximately radial (along rays from 0) with a velocity of V = c/rwhere r is the radial coordinate and c is a constant. If the velocity is 0.5 m/s when r=0.2 m determine: (a) the acceleration magnitude at point A, (b) the acceleration magnitude at point B. 12 m T 0.6 m 0.2 m