FLUID MECHANICS:FUND.+APPL.(LL)>CUSTOM<
FLUID MECHANICS:FUND.+APPL.(LL)>CUSTOM<
3rd Edition
ISBN: 9781260244342
Author: CENGEL
Publisher: MCG CUSTOM
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Chapter 6, Problem 97P

Water flows steadily through a splitter as shown in Fig. P6−97 with V ˙ 1 = 0.08 m 3 / s , V ˙ 2 = 0.05 m 3 / s , D 1 = D 2 = 12 cm, D 3 = 10 cm. If the pressure readings at the inlet and outlets of the splitter are P 1 = 100 kPa, P 2 = 90 kPa and P 3 = 80 kPa, determine external force needed to hold the device fixed. Disregard the weight effects.

Chapter 6, Problem 97P, Water flows steadily through a splitter as shown in Fig. P697 with V1=0.08m3/s , V2=0.05m3/s ,

FIGURE P6−97

Expert Solution & Answer
Check Mark
To determine

The external force needed to hold the device fixed.

Answer to Problem 97P

The final resultant force 254.8N acting at an angle 25.45°.

Explanation of Solution

Given information:

The pressure at pipe 1 is 100kPa, the pressure at pipe 2 is 90kPa, the pressure at pipe 3 is 80kPa, the diameter at pipe 1 and pipe 2 is 12cm, the diameter at pipe 3 is 10cm, the velocity at pipe 1 is 0.08m3/s, the angle θ is 30°, and the velocity at pipe 2 is 0.05m3/s.

The following figure represents the water flows steadily through a splitter.

FLUID MECHANICS:FUND.+APPL.(LL)>CUSTOM<, Chapter 6, Problem 97P

  Figure (1)

Write the expression for the cross-sectional area of pipe 1.

   A1=πd124 ...... (I)

Here, the area of pipe 1 is A1 and the diameter of pipe 1 is d1.

Write the expression for the cross-sectional area of pipe 2.

   A2=πd224 ...... (II)

Here, the area of pipe 2 is A2 and the diameter of pipe 2 is d2.

Write the expression for the cross-sectional area of pipe 3.

   A3=πd324 ...... (III)

Here, the area of pipe 3 is A3 and the diameter of pipe 3 is d3.

Write the expression for the velocity of flow in the pipe 1.

   V1=V˙1A1 ...... (IV)

Here, the velocity of flow in the pipe 1 is V1 and the volume flow rate in the pipe 1 is V˙1.

Write the expression for the velocity of flow in the pipe 2.

   V2=V˙2A2 ...... (V)

Here, the velocity of flow in the pipe 2 is V2 and the volume flow rate in pipe 2 is V˙2.

Write the expression for the velocity of flow in the pipe 3.

   V3=(V˙1V˙2)A3 ...... (VI)

Here, the velocity of flow in pipe 3 is V3 and the volume flow rate pipe 3 is (V˙1V˙2).

Write the expression for resultant force for x components.

   FRx=(V1×cosθ)ρV˙1+ρ(V2)V˙2+P1A1cosθP2A2 ...... (VII)

Here, the resultant force foe x components is FRx, the density of water is ρ, the pressure at pipe 1 is P1, and the pressure at point 2 is P2.

Write the expression for resultant force for y components.

   FRy=(V1×sinθ)ρV˙1ρ(V3)V˙3+P1A1sinθP3A3 ...... (VIII)

Here, the resultant force for y components is FRy and the pressure at point 3 is P3.

Write the expression for net resultant force.

   FR=( F R x )2+( F R y )2 ...... (IX)

Here, the net resultant force is FR.

Write the expression for angle of application of force.

   α=tan1(F R yF R x) ....... (X)

Here, the angle of application is α.

Calculation:

Substitute 12cm for d1 in Equation (I).

   A1=π( 12cm)24=π( 12cm( 1m 100cm ))24=0.0144π4m2=0.011309m2

Substitute 12cm for d2 in Equation (II).

   A2=π( 12cm)24=π( 12cm( 1m 100cm ))24=0.0144π4m2=0.011309m2

Substitute 10cm for d3 in Equation (III).

   A3=π( 10cm)24=π( 10cm( 1m 100cm ))24=0.01π4m2=0.00785m2

Substitute 0.011309m2 for A1 and 0.08m3/s for V˙1 in Equation (IV).

   V1=0.08m3/s0.011309m2=7.074m/s

Substitute 0.011309m2 for A2 and 0.05m3/s for V˙2 in Equation (V).

   V2=0.05m3/s0.011309m2=4.421m/s

Substitute 0.00785m2 for A3, 0.05m3/s for V˙2 and 0.08m3/s for V˙1 in Equation (VI).

   V3=(0.08 m 3 /s0.05 m 3 /s)0.011309m2=0.03m3/s0.011309m2=3.8197m/s

Substitute 1000kg/m3 for ρ, 4.421m/s for V2, 7.074m/s for V1, 90kPa for P2, 100kPa for P1, 0.011309m2 for A1, 30° for θ, 0.011309m2 for A2, 0.05m3/s for V˙2 and 0.08m3/s for V˙1 in Equation (VII).

   F R x =[ ( 7.074m/s ×cos30° )( 1000 kg/ m 3 )( 0.08 m 3 /s ) +( 1000 kg/ m 3 )( 4.421m/s )( 0.05 m 3 /s ) +( 100kPa )( 0.011309 m 2 )( cos30° ) ( 90kPa )( 0.011309 m 2 ) ]

   =[ ( 7.074m/s ×cos30° )( 1000 kg/ m 3 )( 0.08 m 3 /s ) +( 1000 kg/ m 3 )( 4.421m/s )( 0.05 m 3 /s ) +( ( 100kPa )( 1000Pa 1kPa ) )( 0.011309 m 2 )( cos30° ) ( ( 90kPa )( 1000Pa 1kPa ) )( 0.011309 m 2 ) ]

   =[ 489.89 kgm/ s 2 ( 1N 1 kgm/ s 2 )221.05 kgm/ s 2 ( 1N 1 kgm/ s 2 ) +979.381Pa m 2 ( 1N 1Pa m 2 )1017.81Pa m 2 ( 1N 1Pa m 2 ) ]

   =[ 489.89N221.05N-38.429N ]

   FRx=230N

Substitute 1000kg/m3 for ρ, 3.8197m/s for V3, 7.074m/s for V1, 80kPa for P3, 100kPa for P1, 0.00785m2 for A3, 30° for θ, 0.011309m2 for A2, 0.03m3/s for V˙3 and 0.08m3/s for V˙1 in Equation (VIII).

   F R y =[ ( 7.074m/s ×sin30° )( 1000 kg/ m 3 )( 0.08 m 3 /s ) ( 1000 kg/ m 3 )( 3.81m/s )( 0.03 m 3 /s ) +( 100kPa )( 0.011309 m 2 )( sin30° ) ( 80kPa )( 0.0078 m 2 ) ]

   =[ ( 7.074m/s ×sin30° )( 1000 kg/ m 3 )( 0.08 m 3 /s ) ( 1000 kg/ m 3 )( 3.81m/s )( 0.03 m 3 /s ) +( 100kPa )( 1000Pa 1kPa )( 0.011309 m 2 )( sin30° ) ( 80kPa )( 1000Pa 1kPa )( 0.0078 m 2 ) ]

   =[ 282.87 kgm/ s 2 ( 1N 1 kgm/ s 2 )114.32 kgm/ s 2 ( 1N 1 kgm/ s 2 ) +565Pa m 2 ( 1N 1Pa m 2 )624Pa m 2 ( 1N 1Pa m 2 ) ]

   =[ 282.87N114.32N +565N624N ]

   FRy=109.5N

Substitute 109.5N for FRy and 230N for FRx in Equation (IX).

   FR=( 230N)2+( 109.5N)2=52900+11990.25=64829.25=254.8N

Thus, the final resultant force is 254.8N.

Substitute 109.5N for FRy and 230N for FRx in Equation (X).

   α=tan1(109.5N230N)=tan1(0.4760)=25.45°

The final resultant force 254.8N acting at an angle 25.45°.

Conclusion:

The final resultant force 254.8N acting at an angle 25.45°.

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FLUID MECHANICS:FUND.+APPL.(LL)>CUSTOM<

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