Fluid Mechanics

Structural Analysis
6th Edition
ISBN:9781337630931
Author:KASSIMALI, Aslam.
Publisher:KASSIMALI, Aslam.
Chapter2: Loads On Structures
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Fluid Mechanics 

Faculty of Engineering
Department: - Civil Engineering
UNIVERSITY or BISA
Fluid mechanics - Assignment No. 5
1. 80 mm diameter circular pipe carries water at 20°C. Calculate the largest flow rate (Q) which laminar flow
can be expected.( v = 106 m² /s).
2. An oil with p = 900 kg/m³ and v = 0.0002 m2 /s flows upward through an inclined pipe as shown in Fig. 1.
The pressure and elevation are known at sections 1 and 2, 10 m apart. ASsuming steady laminar flow, (a)
verify that the flow is up, (b) compute hf between 1 and 2, and compute (c) Q, (d) V, and (e) Red. Is the
flow really laminar?
d= 6 cm
10 m
Q.V
P2 = 250,000 Pa
40°
P, = 350,000 Pa, z = 0
Fig. 1
3. A liquid of specific weight p g= 58 lbf/ft3 flows by gravity through a 1-ft tank and a 1-ft capillary tube at a
rate of 0.15 ft3 /h, as shown in Fig. 2. Sections 1 and 2 are at atmospheric pressure. Neglecting entrance
effects, compute the viscosity of the liquid.
50cm
50cm
d= 12mm
Q = 0.0041 m³/h
Fig. 2
Transcribed Image Text:Faculty of Engineering Department: - Civil Engineering UNIVERSITY or BISA Fluid mechanics - Assignment No. 5 1. 80 mm diameter circular pipe carries water at 20°C. Calculate the largest flow rate (Q) which laminar flow can be expected.( v = 106 m² /s). 2. An oil with p = 900 kg/m³ and v = 0.0002 m2 /s flows upward through an inclined pipe as shown in Fig. 1. The pressure and elevation are known at sections 1 and 2, 10 m apart. ASsuming steady laminar flow, (a) verify that the flow is up, (b) compute hf between 1 and 2, and compute (c) Q, (d) V, and (e) Red. Is the flow really laminar? d= 6 cm 10 m Q.V P2 = 250,000 Pa 40° P, = 350,000 Pa, z = 0 Fig. 1 3. A liquid of specific weight p g= 58 lbf/ft3 flows by gravity through a 1-ft tank and a 1-ft capillary tube at a rate of 0.15 ft3 /h, as shown in Fig. 2. Sections 1 and 2 are at atmospheric pressure. Neglecting entrance effects, compute the viscosity of the liquid. 50cm 50cm d= 12mm Q = 0.0041 m³/h Fig. 2
Faculty of Engineering
Department: - Civil Engineering
UNIVERSITY or BISA
Fluid mechanics - Assignment No. 2
Fluid Properties
1. Two pipes on the same elevation convey water and oil of specific gravity 0.88 respectively (Figure 1).
They are connected by a U-tube manometer with the manometric liquid having a specific gravity of
1.25. If the manometric liquid in the limb connecting the water pipe is 2 m higher than the other find
the pressure difference in two pipes.
Oil
Water
B.
Figure 1
h-5m
2. In Figure 2 the tank contains water and immiscible oil at 20°C. What is h in centimeters if the density of
the oil is 898 kg/m3?
h
6 ст
12 cm
Oil
Water
8 cm
Figure 2
3. Pressure gage B is to measure the pressure at point A in a water flow (Figure 3). If the pressure at B is
87 kPa, estimate the pressure at A in kPa. Assume all fluids are at 20C.
Ywater = 9790 N/m³:
Ymercury = 133,100 N/m³;
Yoil = 8720 N/m³
SAE 30 oil
Gage B
Mercury
6 cm
5 cm
Water
flow
11 cm
4 cm
Figure 3
Transcribed Image Text:Faculty of Engineering Department: - Civil Engineering UNIVERSITY or BISA Fluid mechanics - Assignment No. 2 Fluid Properties 1. Two pipes on the same elevation convey water and oil of specific gravity 0.88 respectively (Figure 1). They are connected by a U-tube manometer with the manometric liquid having a specific gravity of 1.25. If the manometric liquid in the limb connecting the water pipe is 2 m higher than the other find the pressure difference in two pipes. Oil Water B. Figure 1 h-5m 2. In Figure 2 the tank contains water and immiscible oil at 20°C. What is h in centimeters if the density of the oil is 898 kg/m3? h 6 ст 12 cm Oil Water 8 cm Figure 2 3. Pressure gage B is to measure the pressure at point A in a water flow (Figure 3). If the pressure at B is 87 kPa, estimate the pressure at A in kPa. Assume all fluids are at 20C. Ywater = 9790 N/m³: Ymercury = 133,100 N/m³; Yoil = 8720 N/m³ SAE 30 oil Gage B Mercury 6 cm 5 cm Water flow 11 cm 4 cm Figure 3
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