Connect Access for Fluid Mechanics
Connect Access for Fluid Mechanics
4th Edition
ISBN: 9781259877759
Author: Yunus A. Cengel Dr.
Publisher: McGraw-Hill Education
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Chapter 7, Problem 107P
To determine

Expression showing relationship x-component of fluid velocity.

Expert Solution & Answer
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Answer to Problem 107P

Dimensionless relationship for x-component of fluid velocity is

  uVtopVbottom=f(Re,yh)

Explanation of Solution

Given Information:

Top plate speed, Vtop

Bottom plate speed, Vbottom

Steady flow, incompressible, 2 dimensional.

Concept used:

Buckinghams Pi theorem.

Calculation:

Fluid velocity − u

Distance between parallel plate − h

Distance − y

Fluid density - ρ

Fluid viscosity - μ

Plate speeds − V

No. Pf parameters, n = 6

The relative velocity of the top and bottom plate.

  V =VtopVbottom

Fluid velocity u is the function of remaining five parameters

  u=f(ρ,μ,(VtopVbottom),h,y)

The primary dimension of each parameter.

Velocity,

  {u}={LT}={L1T1}

Density,

  {ρ}={massvolume}={ML3}={M1L3}

Viscosity,

  {μ}={MLT}={M1L1T1}

Distance y,

  {y}={L1}

Distance h,

  {h}={L1}

Plate speeds,

  {VtopVbottom}={LT}={L1T1}

No. Of primary dimensions used in the problem is 3. (M,L,T)

J=3

K=n-j=6-3=3

As per Buckinghams Pi theorem, no. of this π's is = 3

Since j=3, we need to select 3 repeating parameters.

According to the guideline, we should select ρ,h and (VtopVbottom) as a repeating parameter.

(1) Now creating π's by combing repeating parameters with the remaining parameters.

Dependant π

  (π1)=uha1ρb1(VtopVbottom)c1

The primary dimension of the above term is

  {π}={M0L0T0}

  ={uha1ρb1(VtopVbottom)c1}={(L1T1)(L1)(ML3)b1(L1T1)c1}

Now equation becomes,

  {m0L0t0}={(L1T1)(L1)a1(ML3)b1(L1T1)c1}

Equating each primary dimension to solve a1,b1,c1,

Mass,

  {M0}={Mb1}0=b1b1=0

Length,

  {L0}={L1La1L3b1Lc1}0=1+a13b1+c1a1=0

Time,

  {T0}=(T 1T c1)0=1c1c1=1

Putting values a1,b1,c1 in the equation,

  π1=uh0ρ0(VtopVbottom)1

π1=u(VtopVbottom) --------------(1)

(2) Independent π,

  (π2)=μha2ρb2(VtopVbottom)c2

Primary dimensions of the above term

  {π2}={M0L0T0}

  {μha2ρb2(VtopVbottom)c2}={(M1L1T1)(L1)a2(ML3)b2(L1T1)c2}

Now equation becomes,

  {m0L0t0}={(M1L1T1)(L1)a2(ML3)b2(L1T1)c2}

Equating each primary dimension to solve a2,b2,c2

Mass,

  {m0}={M1Mb2}0=1+b1b1=1

Length,

  {L0}={L1La2L3b2Lc2}0=1+a23b2+c2a2=1

Time,

  {t0}=(T 2T c2)0=1c2c2=1

Putting values a2,b2,c2 in the equation

  π2=μh1ρ1(VtopVbottom)1

  π2=μhρ(VtopVbottom)

Equation of π2 is reciprocal of Reynolds number.

μhρ(VtopVbottom)=1Re -----------------(2)

(3) Independent π using y variable.

  π3=yha3ρb3vc3

The primary dimension of above term.

  {π3}=(M0L0T0)

  {yha3ρb3vc3}={(L1)(L1)a3(ML3)b3(L1T1)c3}

Now equation becomes,

  {m0L0t0}={(L1)(L1)a3(ML3)b3(L1T1)c3}

Equating each primary dimension to solve a3,b3,c3

Mass,

  {M0}={Mb3}0=b3b3=0

Time,

  {T0}={Tc3}0=c3c3=0

Length,

  {L0}={L1La3L3b3Lc3}0=1+a33b3+c3a3=1

Putting all the values in the equation,

  π3=yh1ρ0(VtopVbottom)0π3=yh --------------------(3)

Comparing equation (1)(2)(3)

  uhρ(VtopVbottom)=f(Re,yh)

Conclusion:

Thus, we can develop a dimensionless relationship for x-component of fluid velocity which is a function of fluid viscosity μ, plate speeds, distance h, and distance y, density ρ by using Buckingham Pi theorem.

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