Fluid Mechanics: Fundamentals and Applications
Fluid Mechanics: Fundamentals and Applications
4th Edition
ISBN: 9781259696534
Author: Yunus A. Cengel Dr., John M. Cimbala
Publisher: McGraw-Hill Education
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Textbook Question
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Chapter 14, Problem 57EP

Repeat Prob. 14-55E, ignoring all minor losses. How important are the minor losses in this problem? Discuss.

Expert Solution & Answer
Check Mark
To determine

Whether the minor losses are important or not.

Answer to Problem 57EP

The minor losses are important because the volume flow rate is increased by 11% when neglecting the minor losses.

Explanation of Solution

Given Information:

Inner diameter of the duct is 9.06in, the average roughness of the duct is 0.0059in, total length of the duct is 34.0ft, number of elbows is 3 each having minor loss coefficient of 0.21, hood entry loss coefficient is 4.6, loss coefficient is 1.8, given equation for available head is Havialable=HoaV˙2, shutoff head is 2.30in of water column, volume flow rate is 226SCFM, and constant a is 8.5×106in of water column.

Expression for steady energy equation from point 1 in the stagnant air region to point 2 at the duct outlet.

  P1ρg+α1V122g+z1+Hrequired=P2ρg+α2V222g+z2+hL...... (I)

Here, the required head for the fan is Hrequired, the velocity at the section 1 is V1, the pressure at section 1 is P1, the velocity of water at section 2 is V2, the pressure at section 2 is P2, the density of the water is ρ, the elevation at section 1 is z1, the elevation at section 2 is z2, the acceleration due to gravity is g and the total head loss is hL.

Expression for the total head loss.

  hL=fLV22gD...... (II)

Here, the velocity of the air is V, the friction factor is f, the diameter of the pipe is D and the length of the pipe is L.

Expression for Reynolds's number.

  Re=VDv...... (III)

Here, the kinematic viscosity is v.

Expression for relative roughness.

  R=εD....... (IV)

Here, the roughness of the pipe is ε.

Expression for the friction factor.

  1f=2log10(R3.7+2.51Ref)...... (V)

Expression for the volume flow rate.

  V˙=AV...... (VI)

Here, the area of the pipe is A.

Expression for the area of the pipe.

  A=πD24

Substitute πD24 for A in Equation (V).

. V˙=(πD24)V. ...... (VII)

Expression to convert the shutoff head from inches of water column to inches of air column.

  Ho,air=Ho.water×ρwρa...... (VIII)

Here, the density of the water is ρw, the shutoff head is Ho and the density of the air is ρa.

Expression to convert the a from inches of water column to inches of air column.

  aair=awater×ρwρa...... (IX)

Expression for the total head loss.

  hL=fLV22gD+(Ke+nKelbow+Kdamper)V22g...... (X)

Here, the velocity of the air is V, the friction factor is f, the diameter of the pipe is D, the length of the pipe is l, the loss coefficient at the entrance is Ke, the loss coefficient for the elbow is Kelbow, the loss coefficient for the damper is Kdamper and the number of elbow is n.

Calculation:

Refer to the Table-A-9E, "Properties of air at 1 atm pressure" to obtain the density of the air as 0.07392lbm/ft3, the dynamic viscosity of air as 1.242×103lbm/fts, the value of kinematic viscosity as 1.681×104ft2/s.

Substitute Patm for P1, Patm for P2, z for z2, z for z1, and 0 for V1 in Equation (I).

  P atmρg+α1×02g+z+Hrequired=P atmρg+α2V222g+z+hLHrequired=α2V222g+hL+0Hrequired=α2V222g+hL...... (XI)

Substitute 9.06in for D, 32.2ft/s2 fro g and 34ft for L in Equation (II).

  hL=f( 34ft)V22×32.2ft/ s 2×9.06in+=f( 34ft)V264.4ft/ s 2×9.06in( 1ft 12in )=(0.6992)fV2s2/ft

Substitute (0.6992)fV2s2/ft for hL, 32.2ft/s2 fro g, 1.05 for α2 and V For V2 in Equation (X).

  Hrequired=1.05V22×32.2ft/ s 2+(( 0.6992)fV2 s 2/ft)=1.05V264.4ft/ s 2+(( 0.6992)fV2 s 2/ft)=(0.0163+0.6992f)V2s2/ft...... (XII)

Substitute 9.06ft for D and 1.681×104ft2/s for v in Equation (III).

  Re=V×9.06in1.681× 10 4 ft 2/s=V×9.06in1.681× 10 4 ft 2/s( 1ft 12in)=4491.37V

Substitute 0..0059in for ε and 9.06in for D in Equation (IV).

  R=0.0059in9.06in=6.51×104

Substitute 6.51×104 for R, 4491.37V for Re in Equation (V).

  1f=2log10( 6.51× 10 4 3.7+ 2.51 4491.37V× f )...... (XIII)

Substitute 9.06in for D in Equation (VII).

  V˙=( π ( 9.06in ) 2 4)V=( π ( 9.06in( 1ft 12in ) ) 2 4)V=0.4477Vft2

Substitute 2.3ft for Ho,water, 62.24lbm/ft3 for ρw and 0.07392lbm/ft3 for ρa in Equation (VIII).

  Ho,air=2.3ft×62.24lbm/ ft 30.07392lbm/ ft 3=161.38ft

Substitute 8.5×106in/SCFM2 for a, 62.24lbm/ft3 for ρw and 0.07392lbm/ft3 for ρa in Equation (IX).

  aair=( 8.5× 10 6 in/ SCFM 2 )×62.24lbm/ ft 30.07392lbm/ ft 3=( 8.5× 10 6 in/ SCFM 2 )( 1ft 12in )×62.24lbm/ ft 30.07392lbm/ ft 3=5.96×104ft/SCFM2

Substitute 161.38ft for Ho, 5.96×104ft/SCFM2 for aair and 0.4477Vft2 for V˙ in the given available head Equation.

  Havialable=161.38ft(5.96× 10 4ft/ SCFM 2)(0.4477V ft 2)2=161.38ft(5.96× 10 4ft)(0.2004V2 ft 5/ SCFM 2)=[161.38ft(1.1946 V 2× 10 4 ft 5 / SCFM 2 )]...... (XIV)

Since at the operating point the available head and the required head are equal, therefore equate Equation (XIII) and (XIV).

  [161.38ft(1.1946 V 2× 10 4 ft 5 / SCFM 2 )]=[(0.0163+0.6992f)V2s2/ft][161.38ft( 1.1946 V 2 × 10 4 ft 5 / SCFM 2 )( SCFM 2 0.000289 ft 6 / s 2 )]=(0.0163+0.6992f)V2s2/ft[161.38ft(0.413 V 2 s 2 / ft)]=(0.0163+0.6992f)V2s2/ft.(XV)

Solve Equation (XIII) and Equation (XV) to obtain the value of velocity as 18.72ft/s.

Substitute 18.72ft/s for V and 9.06in for D in Equation (VII).

  V˙=( π ( 9.06in ) 2 4)(18.72ft/s)=( π ( 9.06in( 1ft 12in ) ) 2 4)×18.72ft/s=8.3808ft3/s( 1SCFM 0.017 ft 3 /s )=492.99SCFM

Substitute 3 for n, 0.21 for Kelbow, 4.6 for Kentrance, 1.8 for Kdamper, 9.06in for D, 32.2ft/s2 fro g and 34ft for l in Equation (X).

  hL=f( 34ft)V22×32.2ft/ s 2×9.06in+(4.6+3×0.21+1.8)V22×32.2ft/ s 2=f( 34ft)V264.4ft/ s 2×9.06in( 1ft 12in )+(7.03)V264.4ft/ s 2=(0.699f+0.109)V2s2/ft

Substitute (0.699f+0.109)V2s2/ft for hL, 32.2ft/s2 fro g, 1.05 for α2 and V For V2 in Equation (XI).

  Hrequired=1.05V22×32.2ft/ s 2+(0.699f+0.109)V2s2/ft=1.05V264.4ft/ s 2+(0.699f+0.109)V2s2/ft=(8.08+45.033f)×0.0155V2s2/ft...... (XVI)

Substitute 9.06ft for D and 1.681×104ft2/s for v in Equation (III).

  Re=V×9.06in1.681× 10 4 ft 2/s=V×9.06in1.681× 10 4 ft 2/s( 1ft 12in)=4491.37V

Substitute 0..0059in for ε and 9.06in for D in Equation (IV).

  R=0.0059in9.06in=6.51×104

Substitute 6.51×104 for R, 4491.37V for Re in Equation (V).

  1f=2log10( 6.51× 10 4 3.7+ 2.51 4491.37V× f )...... (XVII)

Substitute 9.06in for D in Equation (VII).

  V˙=( π ( 9.06in ) 2 4)V=( π ( 9.06in( 1ft 12in ) ) 2 4)V=0.4477Vft2

Substitute 2.3ft for Ho,water, 62.24lbm/ft3 for ρw and 0.07392lbm/ft3 for ρa in Equation (VIII).

  Ho,air=2.3ft×62.24lbm/ ft 30.07392lbm/ ft 3=161.38ft

Substitute 8.5×106in/SCFM2 for a, 62.24lbm/ft3 for ρw and 0.07392lbm/ft3 for ρa in Equation (IX).

  aair=8.5× 10 6in/ SCFM 2×62.24lbm/ ft 30.07392lbm/ ft 3=( 8.5× 10 6 in/ SCFM 2 )( 1ft 12in )×62.24lbm/ ft 30.07392lbm/ ft 3=8.5×106in/SCFM2

Substitute 161.38ft for Ho, 5.96×104ft/SCFM2 for a and 0.4477Vft2 for V˙ in the given available head equation.

  Havialable=161.38ft(5.96× 10 4ft/ SCFM 2)(0.4477V ft 2)2=161.38ft(5.96× 10 4ft/ SCFM 2)(0.2004V2 ft4)=161.38ft(1.1946V2× 10 4 ft 5/ SCFM 2)...... (XVIII)

Since at the operating point the available head and the required head are equal, therefore equate equation (XVI) and (XVIII).

  [161.38ft( 1.1946 V 2 × 10 4 ft 5 / SCFM 2 )]=[( 8.08+45.033f)×0.0155 V 2 s 2 / ft][161.38ft( 1.1946 V 2 × 10 4 ft 5 / SCFM 2 )( SCFM 2 0.000289 ft 6 / s 2 )]=[( 8.08+45.033f)×0.0155 V 2 s 2 / ft][161.38ft( 0.413 V 2 s 2 / ft )]=[( 8.08+45.033f)×0.0155 V 2 s 2 / ft]...... (XIX)

Solve Equation (XVII) and Equation (XIX) to obtain the value of velocity as 16.8ft/s.

Substitute 16.8ft/s for V and 9.06in for D in Equation (VII).

  V˙=( π ( 9.06in ) 2 4)(16.8ft/s)=( π ( 9.06in( 1ft 12in ) ) 2 4)×16.8ft/s=7.5213ft3/s( 1SCFM 0.017 ft 3 /s )=451.277SCFM

Therefore, the volume flow rate when considering the minor losses is 451.277SCFM and the volume flow rate when the minor losses are neglected is 492.99SCFM. Hence, the volume flow rate is increased by approximately by 11% while neglecting the minor losses. So the minor losses are not negligible.

Conclusion:

The minor losses are important because the volume flow rate is increased by 11% when neglecting the minor losses.

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Chapter 14 Solutions

Fluid Mechanics: Fundamentals and Applications

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