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© Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

© Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

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Page 1: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

© Pritchard

Introduction to Fluid Mechanics

Chapter 8

Internal Incompressible Viscous Flow

Page 2: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

© Pritchard

Main TopicsEntrance RegionFully Developed Laminar Flow

Between Infinite Parallel PlatesFully Developed Laminar Flow in a PipeTurbulent Velocity Profiles in

Fully Developed Pipe FlowEnergy Considerations in Pipe FlowCalculation of Head LossSolution of Pipe Flow ProblemsFlow Measurement

Page 3: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

 Internal Incompressible Viscous Flow

Page 4: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Turbulent flows Fluid particles rapidly mix as they move along due to random

three-dimensional velocity fluctuations. Semi-empirical theories in conjunction with experimental data are the common approach for a turbulent flow. Computational solutions are also available through the use of some empirical parameters, however.

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Page 5: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Turbulent flows in a duct 

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Page 6: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Turbulent flows 

Page 7: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Incompressible flow

 

Page 8: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Velocity profiles for fully developed pipe flow

Page 9: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Energy Consideration in Pipe Flow

Page 10: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Energy Consideration in Pipe Flow

Page 11: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Energy Consideration in Pipe Flow

Use the empirical power-law profile, Eq. 8.22.

Page 12: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Head losses

Page 13: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Head losses

Thermal energy converted from the mechanical energy from 1 to 2

Mechanical energies, pressure, kinetic, and potential energies.

Page 14: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Head losses

Page 15: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Calculation of Head Losses/Major Losses

The mechanical energy loss is primarily due to the friction along a pipe and may be divided into two parts: Frictional loss along a straight ,constant-flow-area pipe and frictional loss due to the change of flow area or path. The first part is called Major Loss and may be evaluated in terms of a horizontal pipe without the effect of elevation. The second part is called Minor Loss and will be discussed later.

Page 17: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Major losses

Page 18: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Friction factor for turbulent flow

Wall roughness affects the friction loss of turbulent flow. Since the wall roughness is random, an effective roughness is determined.

sand size e

eroughnessRandom

Page 19: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

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Page 20: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Calculation of Head losses

Page 21: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

© Pritchard

Moody diagram

Page 22: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Calculation of friction factor

Page 23: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

© Pritchard

Heat losses due to flow area and pass changes/Minor Losses

Minor Losses• Examples: Inlets and Exits; Enlargements and Contractions;

Pipe Bends; Valves and Fittings

Page 24: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

© Pritchard

Calculation of Head Loss

Minor Loss: Loss Coefficient, K

Minor Loss: Equivalent Length, Le

Page 25: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Calculation of Minor losses

TlhgZ

VPgZ

VP )

2()

2( 2

2

2

_

21

2

1

_

1

mT lll hhh

Page 26: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Mechanical energy change of the fluid across the pump

 

Page 27: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

 Mechanical energy change of the fluid across the pump 

 The above equation is only for Mechanical energy change of the fluid across the pump, not a general energy balance!

Page 28: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

Energy balance of a fluid system including a pump

 

Page 29: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

 Energy balance of a fluid system including a pump 

 

Tlinin

pumppipe hm

Wuu

m

Q

m

W

m

Quu

m

Q

)1()()()1()()()( 1212

The above equation may be rewritten as:

lT

pumphgZ

VpgZ

Vp

m

Wor )

2()

2( 1

2

1

_

11

2

2

2

_

22

.

Page 30: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

 Thermal energy balance 

 

Thermal energy balance:

Thermal energy due to the mechanical energy dissipation in the pipeline + thermal energy due to the mechanical energy dissipation in the pump per mass flow rate is equal to:

)( 12 uum

Q

m

Q pumppipe

However the mechanical energy dissipation in the pump = m

Win

)1(

Therefore

Tlinpumppipe h

m

Wuu

m

Q

m

Q

)-(1 )( 12

is the mechanical energy dissipation in the pipeline only, not including that in the pump.

Page 31: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

 Noncircular Ducts

 

Page 32: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

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Page 33: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow

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Page 34: © Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow