FLUID MECHANICS-PHYSICAL ACCESS CODE
FLUID MECHANICS-PHYSICAL ACCESS CODE
8th Edition
ISBN: 9781264005086
Author: White
Publisher: MCG
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Chapter 5, Problem 5.1CP
To determine

To rewrite:

This function in dimensionless form, using dimensional analysis.

Expert Solution
Check Mark

Answer to Problem 5.1CP

The dimensionless function is Cf=fcn(Re,εd)

Explanation of Solution

Given Information:

For long circular rough pipes in turbulent flow, wall shear τw is a function of density ρ, viscosity μ .average velocity V, pipe diameter d and wall roughness height e. Thus it can be written as:

τw=fcn(ρ,μ,V,d,e)

Concept Used:

The number of pi groups are to be calculated:

N=kr

Where k is the number of variables and r is the number of fundamental references.

On substituting 6 for k and 3 for r ,

N=3

Calculation:

Dimensional analysis is applied to find the pi groups.

First pi group:

π1=ρaVbμcd

Where ρ is the density, velocity is V, diameter is d and the dynamic viscosity is μ.

On substituting M0L0T0 for π1, [ML3] for ρ, [LT1] for V and [ML1T1] for μ,

M0L0T0=[ML3]a[LT1]b[ML1T1]c[L]

M0L0T0=[Ma+cL3a+bc+1Tbc]

On equating M coefficients:

a+c=0a=c

On equating T coefficients:

bc=0b=c

On equating L coefficients:

3a+bc+1=03(c)+(c)c+1=0c=1

Hence, a = 1, b = 1

Therefore, the first pi group is as follows:

π1=ρ1V1μ1d

π1=ρVdμ

Second pi group:

π2=ρaVbεcd

Where ρ is the density, velocity is V, diameter is d and roughness height is ε.

On substituting M0L0T0 for π2, [ML3] for ρ, [M0L1T0] for ε and L for d ,

M0L0T0=[ML3]a[LT1]b[M0L1T0]c[L]

M0L0T0=[MaL3a+b+c+1Tb]

On equating M coefficients:

a=0

On equating T coefficients:

b=0b=0

On equating L coefficients:

3a+b+c1=03(0)+0+c1=0c=1

Therefore, the second pi group is as follows:

π2=ρ0V0ε1d1

π2=εd

Third pi group:

π3=ρaVbdcτw

Where ρ is the density, velocity is V, diameter is d and shear stress is τw.

On substituting M0L0T0 for π3, [ML3] for ρ, [LT1] for V, [L] for d, and [ML1T2] for τw,

M0L0T0=[ML3]a[LT1]b[L]c[ML1T2]

M0L0T0=[Ma+1L3a+b+c1Tb2]

On equating M coefficients:

a+1=0a=1

On equating T coefficients:

b2=0b=2

On equating L coefficients:

3a+b+c1=03(1)+(2)+c1=0c=0

Therefore, the third pi group is as follows:

π3=ρ1V2d0τw

π2=τwρV2

Hence as per the choices:

π3=fcn(π1,π2)

On substituting τwρV2 for π3, εd for π2 and ρVdμ for π1,

τwρV2=fcn(ρVdμ,εd)

Where τwρV2 is the skin friction coefficient represented by Cf and ρVdμ is known as Reynolds number represented by Re.

Cf=fcn(Re,εd)

Conclusion:

The dimensionless function is Cf=fcn(Re,εd).

To determine

To plot:

Data using the dimensionless form obtained, a curve fit formula and a single value of a range.

Expert Solution
Check Mark

Answer to Problem 5.1CP

The data is plotted as above, the curve fit formula is Cf=3.63Re0.64 and the curve is valid for only Reynolds number range of 2000-22000 and single ε/d value.

Explanation of Solution

Given Information:

Diameter of pipe, d = 5 cm

ε=0.25mm

The following values of wall shear stress are shown by the measurements for flow of water at 20?:

FLUID MECHANICS-PHYSICAL ACCESS CODE, Chapter 5, Problem 5.1CP , additional homework tip  1

Concept Used:

The parameter ε/d remains constant for all data.

As per the table (Moody chart):

μ=0.001kg/m.s, the dynamic viscosity of water at 20°C

ρ=998kg/m3, the density of water at 20°C

The velocity is calculated as follows:

V=QA

V=Qπ4d2

Reynolds number is calculated as follows:

Re=ρVdμ

The skin friction coefficient is calculated as follows:

Cf=τwρV2

Calculation:

εd=0.2550, because parameter ε/d remains constant for all data.

On substituting 1.5 gal/min for Q and 50 mm for d in the calculation of velocity:

V=1.5gal/min×(6.3094× 10 5m3/s1gal/min)π4d2

V=1.5gal/min×6.3094×105m3/sπ4(50× 10 3)2m2

V=0.0481972m/s

On substituting 998 kg/m3 for ρ, 0.0481972 m/s for V ,50 mm for d and 0.001 kg/m.s for μ in the calculation for Reynolds number:

Re=998×0.0481972×(50×103)μ

Re=48.1008056×(50×103)0.001

=2405

On substituting 0.05 Pa for τw, 998 kg/m3 for ρ and 0.0481972 m/s for V.

Cf=τw998×0.04819722

Cf=0.052.31832415

=0.021567

Remaining values are also calculated similarly and tabulated as follows:

V (m/s) 0.0481972 0.0963944 0.1927888 0.2891832 0.3855776 0.4498406
Re 2405 4810 9620 14430 19240 22447
Cf 0.021567 0.019411 0.009975 0.007668 0.005796 0.00619

The curve is plotted between Cf versus Re:

FLUID MECHANICS-PHYSICAL ACCESS CODE, Chapter 5, Problem 5.1CP , additional homework tip  2

The following equation shows the power law curve fit in the plot:

Cf=3.63Re0.64

R2=0.953

Hence, 95.3% is the correlation.

Hence, the curve is valid for only Reynolds number range of 2000-22000 and single ε/d value.

Conclusion:

The data is plotted as above, the curve fit formula is Cf=3.63Re0.64 and the curve is valid for only Reynolds number range of 2000-22000 and single ε/d value.

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Chapter 5 Solutions

FLUID MECHANICS-PHYSICAL ACCESS CODE

Ch. 5 - Prob. 5.11PCh. 5 - The Stokes number, St, used in particle dynamics...Ch. 5 - Prob. 5.13PCh. 5 - Flow in a pipe is often measured with an orifice...Ch. 5 - The wall shear stress T in a boundary layer is...Ch. 5 - P5.16 Convection heat transfer data are often...Ch. 5 - If you disturb a tank of length L and water depth...Ch. 5 - Prob. 5.18PCh. 5 - Prob. 5.19PCh. 5 - Prob. 5.20PCh. 5 - Prob. 5.21PCh. 5 - As will be discussed in Chap. 11, the power P...Ch. 5 - The period T of vibration of a beam is a function...Ch. 5 - Prob. 5.24PCh. 5 - The thrust F of a propeller is generally thought...Ch. 5 - A pendulum has an oscillation period T which is...Ch. 5 - Prob. 5.27PCh. 5 - Prob. 5.28PCh. 5 - P5.29 When fluid in a pipe is accelerated linearly...Ch. 5 - Prob. 5.30PCh. 5 - P5.31 The pressure drop per unit length in...Ch. 5 - A weir is an obstruction in a channel flow that...Ch. 5 - Prob. 5.33PCh. 5 - Prob. 5.34PCh. 5 - Prob. 5.35PCh. 5 - Prob. 5.36PCh. 5 - Prob. 5.37PCh. 5 - Prob. 5.38PCh. 5 - Prob. 5.39PCh. 5 - Prob. 5.40PCh. 5 - A certain axial flow turbine has an output torque...Ch. 5 - When disturbed, a floating buoy will bob up and...Ch. 5 - Prob. 5.43PCh. 5 - Prob. 5.44PCh. 5 - P5.45 A model differential equation, for chemical...Ch. 5 - P5.46 If a vertical wall at temperature Tw is...Ch. 5 - The differential equation for small-amplitude...Ch. 5 - Prob. 5.48PCh. 5 - P5.48 A smooth steel (SG = 7.86) sphere is...Ch. 5 - Prob. 5.50PCh. 5 - Prob. 5.51PCh. 5 - Prob. 5.52PCh. 5 - Prob. 5.53PCh. 5 - Prob. 5.54PCh. 5 - Prob. 5.55PCh. 5 - P5.56 Flow past a long cylinder of square...Ch. 5 - Prob. 5.57PCh. 5 - Prob. 5.58PCh. 5 - Prob. 5.59PCh. 5 - Prob. 5.60PCh. 5 - Prob. 5.61PCh. 5 - Prob. 5.62PCh. 5 - The Keystone Pipeline in the Chapter 6 opener...Ch. 5 - Prob. 5.64PCh. 5 - Prob. 5.65PCh. 5 - Prob. 5.66PCh. 5 - Prob. 5.67PCh. 5 - For the rotating-cylinder function of Prob. P5.20,...Ch. 5 - Prob. 5.69PCh. 5 - Prob. 5.70PCh. 5 - The pressure drop in a venturi meter (Fig. P3.128)...Ch. 5 - Prob. 5.72PCh. 5 - Prob. 5.73PCh. 5 - Prob. 5.74PCh. 5 - Prob. 5.75PCh. 5 - Prob. 5.76PCh. 5 - Prob. 5.77PCh. 5 - Prob. 5.78PCh. 5 - Prob. 5.79PCh. 5 - Prob. 5.80PCh. 5 - Prob. 5.81PCh. 5 - A one-fiftieth-scale model of a military airplane...Ch. 5 - Prob. 5.83PCh. 5 - Prob. 5.84PCh. 5 - *P5.85 As shown in Example 5.3, pump performance...Ch. 5 - Prob. 5.86PCh. 5 - Prob. 5.87PCh. 5 - Prob. 5.88PCh. 5 - P5.89 Wall friction Tw, for turbulent flow at...Ch. 5 - Prob. 5.90PCh. 5 - Prob. 5.91PCh. 5 - Prob. 5.1WPCh. 5 - Prob. 5.2WPCh. 5 - Prob. 5.3WPCh. 5 - Prob. 5.4WPCh. 5 - Prob. 5.5WPCh. 5 - Prob. 5.6WPCh. 5 - Prob. 5.7WPCh. 5 - Prob. 5.8WPCh. 5 - Prob. 5.9WPCh. 5 - Prob. 5.10WPCh. 5 - Given the parameters U,L,g,, that affect a certain...Ch. 5 - Prob. 5.2FEEPCh. 5 - Prob. 5.3FEEPCh. 5 - Prob. 5.4FEEPCh. 5 - Prob. 5.5FEEPCh. 5 - Prob. 5.6FEEPCh. 5 - Prob. 5.7FEEPCh. 5 - Prob. 5.8FEEPCh. 5 - In supersonic wind tunnel testing, if different...Ch. 5 - Prob. 5.10FEEPCh. 5 - Prob. 5.11FEEPCh. 5 - Prob. 5.12FEEPCh. 5 - Prob. 5.1CPCh. 5 - Prob. 5.2CPCh. 5 - Prob. 5.3CPCh. 5 - Prob. 5.4CPCh. 5 - Does an automobile radio antenna vibrate in...Ch. 5 - Prob. 5.1DPCh. 5 - Prob. 5.2DP
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Unit Conversion the Easy Way (Dimensional Analysis); Author: ketzbook;https://www.youtube.com/watch?v=HRe1mire4Gc;License: Standard YouTube License, CC-BY