10.1: PROBLEM DEFINITION
Situation:
Kerosene ows in a pipe.
Q=0.02 m3/s,D=17.7cm.
Find:
Is the ow laminar or turbulent?
Entrance length (meters).
Properties:
Kerosene (20 C),Table A.4=2.37 ×106m2/s.
SOLUTION
Reynolds number:
Entrance length:
1
10.2: PROBLEM DEFINITION
Situation:
A compressor is drawing ambient air through a duct.
Q=0.3m
3/s,D=0.15 m.
L=10m,T=20C.
Find:
Determine if the ow is laminar or turbulent.
Entrance length (meters).
Assumptions:
Smooth inlet, so Lecorrelations apply.
Pressure in duct is 1.0 atm.
Properties:
Air (20 C,p=1atm), Table A.3, ν=15.1×106m2/s.
SOLUTION
Reynolds number:
Since Re >3000,theow is turbulent.
2
10.3: PROBLEM DEFINITION
Situation:
A tube carries SAE 10W-30 oil.
Q=0.1L/s=0.0002 m3/s,T=38C.
Flow must be laminar and fully developed.
Find:
Specify a tube length (millimeters).
Specify a tube diameter (millimeters).
Assumptions:
Smooth inlet, so Lecorrelations apply.
Properties:
SAE 10W-30 oil (38 C), Table A.4, ν=7.6×105m2/s.
PLAN
1. Find diameter Dby specifying a Reynolds number of 1500 (laminar).
2. Find length Lby specifying a length so L>0.05DRe .
SOLUTION
Reynolds number:.
Entrance length:
Select
3
Problem 10.4
Answer the questions below.
a.) What is pipe head loss? How is pipe head loss related to total head loss?
Pipe head loss ==>head loss associated with fully developed ow in straight
b.) What is the friction factor f?Howisfrelated to wall shear stress?
fis a π-group
c.) What assumptions need to be satised to apply the Darcy Weisbach equation?
the conduit needs to be completely full of the owing uid
4
Problem 10.5
Apply the grid method to each situation described below. Apply the Darcy Weisbach
equation. Note: Unit cancellations are not shown in this solution.
Situation:(a)
Water is owing in a pipe.
Q=20gpm, V=180ft/min.
L=200ft,f=0.02.
Find:
Head loss (ft).
Solution:
Flow rate eqn:
Situation:(b)
Flow in a PVC pipe.
hf=0.8m,f=0.012,L=15m Q=2ft
3/s..
Find:
Pipe diameter (meters).
Solution:
5
10.6: PROBLEM DEFINITION
Situation:
SITUATION
Air is owing from a large tank to ambient through a horizontal pipe.
Pipe is 1″ Schedule 40. D=1.049 in = 0.0266 m.
V=10m/s.f=0.015,L=50m.
Assumptions:
Air has constant density (look up properties at 1 atm).
KE correction factor is a2=1.0.
Properties:
Air (20 C,1atm,Table A.3): ρ=1.2kg/m3.
PLAN
1. Relate pressure in tank to head loss using the energy equation.
2. Describe head loss using the Darcy-Weisbach equation.
3. Combine steps 1 & 2.
SOLUTION
1. Energy eqn. (location 1 inside the tank, location 2 at the pipe exit)
2. Darcy-Weisbach eqn.:
3. Combine Eqs. (1) and (2).
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REVIEW The constant density assumption is valid because the pressure in the tank
is less than 2% of atmospheric pressure.
7
10.7: PROBLEM DEFINITION
Situation:
Water is owing through a horizontal pipe (garden hose).
D=0.022 m,L=20m.
f=0.012,V=2.0m/s.
Find:
Pressure drop (Pa) for 20 m of hose.
Properties:
Water (15 C), Table A.5, ρ= 999 kg/m3.
PLAN
1. Relate pressure drop to head loss using the energy equation.
2. Describe head loss using the Darcy-Weisbach equation.
3. Combine steps 1 & 2.
SOLUTION
1. Energy eqn. (location 1 upstream; location 2 is 20 m downstream)
2. Darcy-Weisbach eqn.:
3. Combine Eqs. (1) and (2):
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10.8: PROBLEM DEFINITION
Situation:
Water is owing from a tank through a tube & then discharging to ambient.
D=0.008 m,L=6m.
H=3m,f=0.015.
Sketch:
Find:
Exit velocity (m/s).
Discharge (L/s).
Sketch the HGL & EGL.
Assumptions:
Theonlyheadlossisinthetube.
Turbulent ow so α2=1.0.
Properties:
Water (15 C), Table A.5 (EFM10e), ρ=999kg/m3ν=1.14 ×106m2/s.
PLAN
1. Relate Hto head loss using the energy equation.
2. Describe head loss using the Darcy-Weisbach equation.
3. Find Vby combining steps 1 & 2.
4. Find Qby using the ow rate equation.
SOLUTION
1. Energy eqn. (location 1 at the free surface, location 2 at the pipe exit)
2. Darcy-Weisbach eqn.:
9
3. Combine Eqs. (1) and (2):
4. Flow rate equation:
5. Sketch HGL & EGL
Locate the EGL & HGL on free surface of tank.
Locate the EGL and HGL at the end of the pipe. Sketch lines.
REVIEW Check the turbulent ow assumption.
Thus, the assumption of turbulent ow is valid.
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10.9: PROBLEM DEFINITION
Situation:
Water ows through a pipe.
V=3m/s,z1=10m.
z2=11m,D=5cm
Sketch:
Find:Resistancecoecient, f.
SOLUTION
Manometer equation
Darcy Weisbach
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10.10: PROBLEM DEFINITION
Answer the questions below.
a. What are the main characteristics of laminar ow?
Flow in layers
b. What is the meaning of each variable that appears in Eq. (10.27)?
Vis the area-averaged velocity in the pipe; also called the mean velocity
c. In Eq. (10.33), what is the meaning of hf?
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10.11: PROBLEM DEFINITION
Situation:
Fluid owing in a pipe.
V=0.04 m/s,D=0.1m.
Find:
(a) Reynolds number.
(b) Maximum velocity in the pipe.
(c) Friction factor f.
(d) Shear stress at the wall.
(e) Shear stress 25 mm from pipe center.
Properties:μ=10
2Pa ·s=800kg/m3
SOLUTION Reynolds number:
Therefore, the ow is laminar:
Wall shear stress (from denition of f):
13
14
10.12: PROBLEM DEFINITION
Situation:
Water is owing in a pipe. Re = 1000,T=15C.
Nominal diameter = 1/2″ Schedule 40. D=0.622 in = 0.0158 m.
Find:
(a) Mass ow rate (kg/s).
(b) Friction factor f.
(c) Head loss per meter of pipe length.
(d) Pressure drop per meter of head length.
Properties:Water(15 C,1atm), Table A.5, ρ=999kg/m3=9800N/m3=
1.14 ×106m2/s=1.14 ×103N·s/m2.
PLAN
1. Find Vby using known Re.
2Find˙mby using ˙m=ρAV.
3. Find fby using 64/Re.
4. Find hLby using DarcyWeisbach eqn.
5. Find pby using the energy eqn.
SOLUTION
1. Reynolds Number:
2. Mass ow rate:
15
4. Darcy-Weisbach Eqn.:
5. Energy eqn.
KE terms cancel.
Assume horizontal pipe.
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10.13: PROBLEM DEFINITION
Situation:
Liquid ows through a smooth pipe.
V=0.5m/s.h
f=2m per m,D=0.025 m.
Find:
Friction factor.
Reynolds number.
Prove that doubling the ow will double the head loss.
Assumptions:
Laminar ow.
Fully developed ow.
PLAN
1. Find fusing the Darcy-Weisbach eqn.
2. Find Re using f=64/Re .
3. Determine the eect of doubling Qby logical reasoning with the head loss eqn.
SOLUTION
1. Darcy-Weisbach:
2. Assume laminar ow:
3. Head loss in laminar ow
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10.14: PROBLEM DEFINITION
Situation:
Air ows through a round tube.
D=0.0005 m,L=0.75 m.
p2=1.5inch H20 = –373 Pa gage.
Sketch:
Find:
Velocity in the tube (m/s).
Assumptions:
Fully developed ow.
Laminar ow.
Only source of head loss is ow in tube.
Properties:
Air (20 C,1atm), Table A.3, μ=1.81 ×105N·s/m2=15.1×106m2/s.
PLAN
1. Relate velocity to pressure using the energy equation.
2. Find head loss.
3. Find velocity by combining steps 1 and 2.
4. Check laminar ow assumption by calculating Re.
SOLUTION
1. Energy eqn (point 1 back from tube inlet; point 2 at tube outlet):
18
3. Combine Eq. (1) and (2):
(0.0005 m)2
Solve using quadratic equation:
4. Reynolds number:
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10.15: PROBLEM DEFINITION
Situation:
Liquid ows in a vertical pipe; ow direction is unknown.
D=0.008 m.
Sketch:
Find:
Direction of ow.
Velocity (m/s).
Properties:
γ=10kN/m3=3.0×103N·s/m2.
PLAN
1. Find the ow direction by calculating the piezometric head at locations 1 and 2.
2. Find head loss using the energy eqn.
3. Find velocity by using the equation for head loss in laminar ow.
SOLUTION
1. Piezometric Head (location 1 at z=10m):
20