Connect 1 Semester Access Card For Fluid Mechanics Fundamentals And Applications
Connect 1 Semester Access Card For Fluid Mechanics Fundamentals And Applications
3rd Edition
ISBN: 9780077670245
Author: CENGEL
Publisher: McGraw-Hill Education
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Chapter 8, Problem 82P

Water to a residential area is transported at a rate of 1.5 m 3 /s via 70-cm-internal-diameter concrete pipes with a surface roughness of 3 mm and a total length of 1500 m.

In order to reduce pumping power requirements, it is proposed to line the interior surfaces of the concrete pipe with 2-cm-thick petroleum-based lining that has a surface roughness thickness of 0.04 mm. There is a concern that the reduction of pipe diameter to 66 cm and the increase in average velocity may offset any gains. Taking ρ = 100 kg/m 3 and v = 1 × 10 6 m 2 /s for water, determine the percent increase or decrease in the pumping power requirements due to pipe frictional losses as a result of lining the concrete pipes.

Expert Solution & Answer
Check Mark
To determine

The increase or decrease of percent in the pumping power requirements due to pipe frictional losses as a result of lining concrete pipes.

Answer to Problem 82P

The percent decrease in the pumping power requirements is 54.12% .

Explanation of Solution

Given information:

The volume flow rate is 1.5m3/s, the internal diameter of the pipe is 70cm, the surface roughness thickness of the pipe is 3mm, the total length of the pipe is 1500m, the thickness of petroleum based lining in the pipe is 2cm, the surface roughness thickness of the petroleum based lining is 0.04mm, the reduction of pipe diameter is 66cm, the density of water is 1000kg/m3, and the kinematic viscosity of water is 1×106m2/s.

Write the expression for the cross-sectional area of pipe without coating.

   AC=π4D2 ...... (I)

Here, the internal diameter of the pipe is D.

Write the expression for the average velocity of flow in the pipe.

   V=˙AC ...... (II)

Here, the volume flow rate of water is ˙, and the cross-sectional area of pipe is AC.

Write the expression for finding the Reynolds number.

   Re=VDv ...... (III)

Here, the kinematic viscosity is v, average velocity of flow in the pipe is V, and the internal diameter of the pipe is D.

Write the expression for the Colebrook relation of the friction factor for turbulent flow.

   1f1=0.2log(ε/D3.7+2.51Ref1) ...... (IV)

Here, the friction factor is f, the Reynolds number is Re ,and the surface roughness of the pipe is ε.

Write the expression for the head loss in the pipe1.

   hL=f1LDV22g ...... (V)

Here, the length of the pipe is L, the acceleration due to gravity is g ,and the average velocity of flow in the pipe is V.

Write the expression for the new diameter of the pipe with the lining.

   Dr=D2t ...... (VI)

Here, the thickness of the pipe is t, and the internal diameter of the pipe is D.

Write the expression for the new cross-sectional area of the pipe.

   AC=π4Dr ....... (VII)

Here, the new diameter of the pipe with the lining is Dr.

Write the expression for the new average velocity.

   Vr=˙AC ...... (VIII)

Here, the new cross-sectional area of the pipe is AC.

Write the expression for finding the Reynolds number.

   Re=VrDrv ...... (IX)

Here, the new average velocity is Vr.

Write the expression for the new friction function from the Colebrook relation.

   1f2=0.2log(ε2/Dr3.7+2.51Ref2) ...... (X)

Here, the Reynolds number is Re, the surface roughness of the lining is ε2.

Write the expression for finding the new head loss.

   hL=f2LDrVr22g ...... (XI)

Write the expression for the percentage reduction.

   %reduction=hLhL×100 ...... (XII)

Here, the new head loss is hL, and the head loss is hL.

Calculation:

Substitute 70cm for D in the Equation (I).

   AC=π4(70cm( 1m/ 100cm))2=π4(0.7m)2=0.3848m2

Substitute 1.5m3/s for ˙, and 0.3848m2 for AC in the Equation (II).

   V=1.5m3/s0.3848m2=3.8976m/s

Substitute 1×106m2/s for v, 70cm for D, and 3.8976m/s for V in the equation (III).

   Re=(3.8976m/s)(70cm)1×106m2/s=(3.8976m/s)(70cm( 1m 100cm ))1×106m2/s=(3.8976m/s)(0.7m)1×106m2/s=2.7283×106

Substitute 3mm for ε, 70cm for D, and 2.7283×106 for Re in the Equation (IV).

   1f1=0.2log( 3mm/ 70cm 3.7+ 2.51 2.7283× 10 6 f 1 )1f1=0.2log( 3mm( 1m 1000mm )/ 70cm( 1m 100cm ) 3.7+ 2.51 2.7283× 10 6 f 1 )1f1=0.2log(1.1583×103+9.1996× 10 7 f 1 )f1=0.029

Substitute 0.029 for f1, 1500m for L, 70cm for D, 3.8976m/s for V, and 9.81m/s2 for g in the Equation (V).

   hL=0.029(1500m70cm)( ( 3.8976m/s )22( 9.81m/ s 2 ))=0.029(1500m70cm( 1m 100cm ))( ( 3.8976m/s )22( 9.81m/ s 2 ))=0.029(1500m0.7m)(0.77427m)=48.11m

Substitute 70cm for D, and 2cm for t in the Equation (VI).

   Dr=70cm2(2cm)=70cm(1m100cm)2(2cm)(1m100cm)=0.7m(2×0.02m)=0.66m

Substitute 0.66m for Dr in the Equation (VII).

   AC=π4(0.66m)2=π4(0.4356m2)=0.3421m2

Substitute 1.5m3/s for ˙, and 0.3421m2 for AC in the Equation (VIII).

   Vr=1.5m3/s0.3421m2=4.384m/s

Substitute 1×106m2/s for v, 0.66m for Dr, and 4.384m/s for Vr in the equation (IX).

   Re=(4.384m/s)(0.66m)1×106m2/s=2.89344m2/s1×106m2/s=2.894×106

Substitute 0.04mm for ε, 0.66m for Dr, and 2.894×106 for Re in the Equation (X).

   1f2=0.2log(0.04mm/0.66m3.7+2.512.894× 106 f 2 )1f2=0.2log( 0.04mm( 1m 1000mm )/ 0.66m 3.7+ 2.51 2.894× 10 6 f 2 )1f2=0.2log(4× 10 5m3.7+2.512.894× 106 f 2 )1f2=0.2log(1.08108×105+8.6731× 10 7 f 2 )

   f2=0.0117

Substitute 0.0117 for f2, y 1500m for 13 L, 0.66m for Dr,

   4.384m/s for Vr, and 9.81m/s2 for g in the Equation (XI).

   hL=0.0117(1500m0.66m)( ( 4.384m/s )22( 9.81m/ s 2 ))=0.0117(2272.72m)(0.2234m)=26.04m

Substitute 26.04m for hL, and 48.11m for hL in the Equation (XII).

   %reduction=26.04m48.11m×100=0.54125×100=54.12%

Conclusion:

The percent decrease in the pumping power requirements is 54.12% .

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Chapter 8 Solutions

Connect 1 Semester Access Card For Fluid Mechanics Fundamentals And Applications

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