FE Review - Fluids - Spring 2013 - handout...Circular Pipe Flow Open Channel Re < 500 laminar flow...
Transcript of FE Review - Fluids - Spring 2013 - handout...Circular Pipe Flow Open Channel Re < 500 laminar flow...
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Fundamentals of Engineering (FE) Exam
Fluid Mechanics Review
Steven Burian Civil & Environmental Engineering
March 22, 2013
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Morning (Fluid Mechanics) A. Flow measurement B. Fluid properties C. Fluid statics D. Energy, impulse, and momentum equations E. Pipe and other internal flow
7% of FE Morning Session
Up to 15% of FE Afternoon Session
Afternoon (Depends on Discipline) A. Bernoulli equation and mechanical energy balance B. Hydrostatic pressure C. Dimensionless numbers (e.g., Reynolds Number) D. Laminar and turbulent flow E. Velocity head F. Friction losses (e.g., pipes, valves, fittings) G. Pipe networks H. Compressible and incompressible flow I. Flow measurement (e.g., orifices, Venturi meters) J. Pumps, turbines, and compressors K. Non-Newtonian flow L. Flow through packed beds
Fluids and FE
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Fluids § Fluids - substances in liquid or gas
phase
§ Fluids cannot support shear; they deform continuously to minimize applied shear forces
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Viscosity § Shear stress (τ): force required to slide one
unit area layer of a substance over another § Viscosity (µ): measure of a fluid’s resistance
to flow when acted upon by an external force (i.e., ease with which a fluid pours)
§ As a fluid moves a shear stress is developed in it; magnitude is dependent on viscosity of fluid
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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F/A is the fluid shear stress (τ) and the constant of proportionality is the absolute viscosity (µ):
dydu
µτ =
Newtonian fluids: strains are proportional to the applied shear stress
Non-Newtonian fluids: fluid shear stress can be computed using the power law
The kinematic viscosity is the ratio of the absolute viscosity to mass density: ρ
µν =
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Surface Tension § “skin” that seems to form on free surface of a
fluid; caused by intermolecular cohesive forces and is known as surface tension, σ
§ Surface tension - tensile force between two points a unit distance apart on the surface
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Capillarity § Capillary action: caused by surface tension
between liquid and a vertical solid surface § Adhesive forces between liquid molecules and
surface > cohesive forces between liquid molecules; in water, adhesive forces cause fluid to attach itself to and climb solid vertical surface
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Pressure
§ Hydrostatic pressure: pressure of fluid on immersed object or container walls
§ Pressure = force per unit area of surface:
AFP =
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Pressure § Gage pressure: measured relative to a reference
pressure - typically local atmospheric pressure § Absolute pressure: measured relative to a
perfect vacuum § Absolute, gage, and atmospheric pressure are
related as follows:
Pabs = Pgage + Patm
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Pressure
Munson et al. (2002)
P1 abs
P1 gage
P2 gage
P2 abs
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Hydrostatic Pressure
ΔP = change in pressure γ = specific weight of fluid Δh = change in depth in fluid
ΔP = γΔh
***Incompressible fluid at rest
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Manometry § Measure pressure or pressure
differences § Differential manometers: both ends
connected to pressure sources § Open manometers: one end open
to the atmosphere
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Barometers
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Buoyancy
Buoyant force = weight of fluid displaced and is directed vertically upward (Archimedes’ Principle):
Fb = γVd
where Fb = buoyant force γ = specific weight of fluid Vd = displaced volume of fluid
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Displaced volume
Displaced Volume
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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§ If object at rest in fluid, then use equation of static equilibrium in vertical direction, ΣFy = 0
§ Buoyant force passes vertically through centroid of displaced volume; called the center of buoyancy.
Solving Buoyancy Problems
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Fluid Forces on Surfaces
§ Pressure on horizontal plane is uniform over surface
§ Resultant force of pressure distribution acts through center of pressure of surface and is:
PAR =R = resultant vertical force P = pressure on horizontal surface A = area of submerged horizontal surface
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Fluid Forces on Surfaces
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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AhAPR cavg γ== cc
xcR y
AyIy += c
c
xycR x
AyI
x +=
θ O
Free Surface
dF
h hC
A
dA
R
x
y
y
¤ Centroid, c
yc
yR
¤ Center of Pressure, CP
Fluid Forces on Surfaces
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Laminar and Turbulent Flow Laminar Flow:
§ Relatively low velocities § No mixing or a very small degree
of mixing § Fluid appears to flow in
continuous layers with no interaction between the layers
§ Relatively high velocities § High degree of mixing § Fluid motion appears chaotic
Turbulent Flow:
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Flow Distribution
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Reynolds Number
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Reynolds Number
Re < 2000 laminar flow 2000 < Re < 4000 transition region Re > 4000 turbulent flow
Circular Pipe Flow
Open Channel
Re < 500 laminar flow 500 < Re < 2000 transition region Re > 2000 turbulent flow
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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One-Dimensional Flows
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Bernoulli Equation
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Mechanical Energy Equation
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Friction Loss
Valid for laminar and turbulent flow
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Moody Chart
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Minor Loss
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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HGL and EGL
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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HGL and EGL
Z = 0
Total Head or Energy Grade Line
(EGL)
Elevation Head (z)
Velocity Head (v2/2g)
Pressure Head (P/γ)
Hydraulic Grade Line
HGL
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Pump-Turbines
g2vzPhh
g2vzP 2
22
2Ls
21
11 ++=−+++
γγ
Net head added to system by mechanical device
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Open Channel & Pipe Flow
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Impulse-Momentum
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Impulse-Momentum
x111x222x vQvQF ρρΣ −=
y111y222y vQvQF ρρΣ −=
z111z222z vQvQF ρρΣ −=
Sum of the external forces
Net rate of momentum entering control volume
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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Pipe Networks
FE Fluids Review
Fluid Properties
Fluid Statics
Fluid Dynamics
Energy, Friction Loss, and Pipe Flow
Momentum and Drag
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