solve Water, with a kinematic viscosity of 1.21x105 square feet/second, flows from reservoir A to B as shown in thefigure. The pipe has a roughness height of 0.0005-feet, flowrate of 26 cfs, elbows with loss coefficients of 0.2,and a friction factor of 0.019.a) Determine the pipe diameter.b) Sketch the EGL and HGLElevation z₂ = 0(2)BElevation z₁ = 44 ft(1)Total length = 1700 ft

Step 1:Note- Diameter from the last equation, I have calculated with the help of calculator. please…

Answered: Water, with a kinematic viscosity of…

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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Which of the following statements about HGL and EGL is correct? O For any pipe will a constant wall thickness, the slopes of EGL and HGL will be constant. O If the EGL falls below the pipe, then pressure head is negative, indicating a potential location of cavitation. O When a flow passage decreases in diameter, the distance between the EGL and HGL will increase. O When a pipe discharges into the atmosphere, both HGL and EGL will coincide with the system because pressure head is zero at these points.
In the figure shown, the pipe entrance is sharp-edged, and the flow of water is 4 L/s. What is the total minor loss in the pipe? Use a roughness value of 0.25 mm for the cast iron pipe and a value of 1 x 10-6 m²/s for the kinematic viscosity of water. V Water 40 m O a. 13.88 m O b. 2.12 m O c. 2.22 m O d. 13.11 m Turbine Cast iron: L = 125 m, D = 5 cm Open globe valve
. Determine the surface tension in a tube with 0.2m radius and wetting angle 80 and capillary rise of 5mm in N/m and in lb/ft.
Solve for the water discharges in cach steel pipe as shown in Figure 3. You may assume that the minor losses (entrance, exit & bend losses) are negligible. Two trials are enough for this exam. -Elevation 35 m Pipe 1: D-0.2m, L=2400m, f=0.020 Elevation 30 m Elevated tank A -Elevation 28 m Elevated tank B Reservoir C Pipe 3: D=0.15m, L=1500m, f=0.020 Pipe 2: D=0.2m, L=2400m, f=0.020 -Elevation 10 m Figure 3
Q2. Oil with an absolute viscosity of 0.125 N.s/m² and a density of 890 kg/m' is flowing in a 16.5 cm diameter pipe at a 7.5 L/s flow rate. • The fully developed flow is expected to start after.. ... m of pipe entrance.. • plot the shear stress within the pipe cross section.
The rate of flow in a 300mm diameter pipe is 226 liters/seconds. The flow is known to be turbulent. The centerline velocity is 3.66m/s. The density of liquid is given to be 900kg/m. Determine the following: a.) Friction factor; b.) Headloss per meter length of pipe; c.) Shearing stress at the walls of the pipe lee lowe
SUBJECT IS HYDRAULICS SHOW DETAILED AND COMPLETE SOLUTION USED 3 DECIMALS FOR THE FINAL ANSWER The open tank contains two different liquids as shown below. Determine the total pressure at elevation zero. =1.3 A B ELEV. 4.5 m Liquid A spgr = 0.9 ELEV 1.0 m Liauid B spgr = 1.1 El. 0m %3D
Compute the head loss (in meters) in 2000 m of horizontal, steel pipe with nominal pipe size of 300 mm and SCH 30. The pipe is carrying water with an average velocity of 1.88 m/s. Take water at 20°C to have a viscosity of 1.00E-3 Pa-s and density of 1000 kg/(m^3). Take the roughness of steel pipe to be 0.048 mm. Round your answer to 2 decimal places.
The velocity distribution in a pipeline is prescribed by the relation "u=2y-y^2", where 'u" denotes the velocity at a distance y from the solid boundary. Calculate the shear stress at the wall. (Assume coeffiecient of viscosity u= 0.4 poise)
The velocity distribution in a pipeline is prescribed by the relation "u=2y-y^2", where 'u' denotes the velocity at a distance y from the solid boundary. Calculate the shear stress at the wall. (Assume coefficient of viscosity u = 0.4 poise)
The pressure at point 2 shown in Figure is not to fall below 4.14 Bar when the flowrate from the tank is 0.028 m^3/ sec. Determine the minimum height, h, of the water tank under the assumption that (a) minor losses are negligible, (b) minor losses are not negligible. 3 m Figure No.3 Kentrance = 0.5 h The pipe is plastic of 15 cm diameter and (e/D=D0) 1.8 m (2) Main line 450 m with 15 elbows of 90 degree
The compressible flow is assumed to be..?

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