Universidad San Ignacio de Loyola FC-CIV HIDRCANA:...
Transcript of Universidad San Ignacio de Loyola FC-CIV HIDRCANA:...
Eusebio Ingol Blanco, Ph.D. A.M.ASCE
Civil Engineering Program, San Ignacio de Loyola University
Universidad San Ignacio de Loyola
FC-CIV HIDRCANA: Channel Hydraulics Flow Mechanics Review
Objective
• Review the basic concepts of fluid
mechanics
• Recognize the various types of hydraulic
problems
Channel Hydraulics
Channel Hydraulics
Flow in pipes Open channel flow
Applications: Hydraulic structures design
Advance open channel flow, design of pipe
networks, etc.
Pumps
Motivation for Channel Hydraulics
• River Hydraulics and
• Water Resources
• Hydrodynamics
• Groundwater Hydraulics
• Etc.
Experimental Hydraulics
• Oregon State University Wave Research Laboratory
• Model-scale experimental facilities
– Tsunami Wave Basin
– Large Wave Flume
• Dimensional analysis (Chapter 7 ) is very important in designing a model experiment which represents physics of actual problem
What is a fluid?
• A fluid is a substance in the liquid or gaseous form
• Distinction between a solid and a fluid is made on the basis of the substance's ability to resist an applied shear stress that tends to change its shape. – Solid: can resist an applied shear by deforming.
Stress is proportional to strain
– Fluid: deforms continuously under applied shear. Stress is proportional to strain rate
F
A
F V
A h
Solid Fluid
Normal and Shear Stress
• Stress is defined as the force per unit area.
• Normal component called normal stress: – In a fluid at rest, the normal
stress is called pressure
• Tangential component called shear stress
dA
FsShearstres
dA
FssNormalstre
t
n
:
:
The No-Slip Condition
• No slip condition. A fluid in contact with a solid “sticks” to the surface due to viscous effects.
• The fluid property responsible for the no-slip and the development of the boundary layer condition is viscosity
• The flow region adjacent to the wall in which the viscous effects are significant is called the boundary layer.
• the no slip condition is responsible for the development of the velocity profile.
Classification of Fluid Flows
• Internal vs. External Flows
• Internal flows: flows in which the fluid is completely bounded by solid surface. e.g. flow in a pipe or duct
• Flows are dominated by the influence of viscosity throughout the flow field.
• External flows: flows in which the fluid is unbounded over solid surfaces. e.g. flow over a plate, sphere object.
• viscous effects are limited to boundary layers near solid surfaces and to wake regions downstream of bodies.
External flow over a tennis ball, and
the turbulent wake region behind.
Classification of Fluid Flows
• Compressible vs. Incompressible Flow
• Incompressible flow: density remains nearly constant throughout. The volume of each portion of fluid remains unchanged over the course of its motion.
• Liquids flows are typically incompressible
• Compressible flow: density changes of the fluid is significant
• Gas flows are often compressible, especially for high speeds
Classification of Fluid Flows
• Laminar vs. Turbulent Flow
• Laminar Flow: highly ordered fluid motion with smooth stream lines.
• Turbulent flow: highly disordered fluid motion (with high velocities characterized by velocity fluctuations and eddies.
• Transitional flow: a flow that alternates between laminar and turbulent.
Classification of Fluid Flows
• Reynolds number
DVDV
forcesVicous
forcesInertial avgavgRe
Laminar flow Re <2000
Transitional flow 2000 < Re <4000
Turbulent flowRe > 4000
1880, Osborne Reynolds
Classification of Fluid Flows
• Steady vs. Unsteady flow
• Steady Flow implies no change of properties, velocity, pressure, temperature, etc. at a point with time. Transient term in the N-S equation are zero:
• Unsteady flow fluid properties change at a point with time.
- Transient usually describes a starting, or developing flow.
- Periodic refers to a flow which oscillates about a steady
mean.
T1 = 2s
V1 = 3 m/s T2 = 5s
V2 = 3 m/s
Classification of Fluid Flows • Steady vs. Unsteady flow
• Unsteady flow fluid properties change at a point with time.
- Transient usually describes a starting, or developing
flow.
• Uniform vs. Non-Uniform flow
• Uniform flow, flow depth and velocity remain constant with location over a specific region.
• Non-Uniform flow, flow depth changes with distance in the flow direction (flow varied).
T1 = 2s
V1 = 3 m/s T2 = 5s
V2 = 4 m/s
Classification of Fluid Flows
• Steady Uniform Flow: conditions do not change with location in the stream and with time, eg. the flow of water in a pipe of constant diameter at constant velocity.
• Steady non-uniform flow: conditions change from point to point in the stream but remain constant with time
• Unsteady uniform flow: At a given instant (time), the conditions at every point are the same, but will change with time
• Unsteady non-uniform flow: Every condition of the flow changes from point to point and with time at every point.
System and Control Volume
• A system is defined as a quantity of matter or a region in space chosen for study.
• A closed system consists of a fixed amount of mass.
• An open system, or control volume, is a properly selected region in space.
• In chapeter 6, we'll discuss control volumes in more detail.
Density
• Density is defined as mass per unit volume
• In general depends on temperature and pressure.
• Liquids and solids are essentially, incompressible
substances, and the variation of its density with the
pressure is usually negligible.
V
m
VV
*lim
)/( 3mkgV
m
Specific Gravity
• Specific gravity (SG) or relative density is
defined as the ratio of the density of a substance
to the density of some standard substance at a
specified temperature (usually water at 4°C,
with H20= 1000 kg/m3)
SG=/H20
• SG is a dimensionless quantity
3/9790 mkgSG
liquid
water
liquidliquid
SG for water at 20 oC and 1 atm = 1
Specific Weight
• Specific Weight is defined as the weight per unit volume
• where g is the gravitational acceleration
• (e.g., @ 20 oC, 1 atm)
gwater = (998 kg/m3)(9.807 m2/s)
= 9790 N/m3
gair = (1.205 kg/m3)(9.807 m2/s)
= 11.8 N/m3
]/[]/[ 33 ftlbformNgg
?/ 3ftlbf
Density of Ideal Gases
• Equation of State equation for the relationship between pressure, temperature, and density.
• P v = R T
– Rn = universal gas constant = 8.314 kj/kmol . k
– M = molecular weight of the gas
– P is the absolute pressure, v is the specific volume, T is the thermodynamic temperature, R is the gas constant
MRRRTP n /,
Example 2-2
• Given: Natural gas
– Time 1: T1=10oC, p1=200 kPa
– Time 2: T2=10oC, p2=300 kPa
• Find: Ratio of mass at time 2 to that at time 1
– Ideal gas law (p is absolute pressure)
Source: example from lecture Dr. Daene McKinney, The University of Texas at Austin, USA
http://www.ce.utexas.edu/prof/mckinney/ce319f/assign.html
VRT
pVM
1
2
1
2
1
2
p
p
VRT
p
VRT
p
M
M
5.1200
300
1
2 kPa
kPa
M
M
Vapor Pressure and Cavitation
Universidad San Ignacio de Loyola Eusebio Ingol Blanco, Ph.D.
• Vapor Pressure, Pv , is defined as the pressure exerted by
its vapor in phase of equilibrium with its liquid at a
given temperature.
• If P drops below Pv, liquid is locally vaporized, creating
cavities of vapor.
• Vapor cavities collapse when local P rises above Pv.
• Cavitation is noisy, and can cause structural vibrations.
Coefficient of Compressibility
Universidad San Ignacio de Loyola Eusebio Ingol Blanco, Ph.D.
• The volume or density of a fluid changes with a change in its temperature or pressure.
• Fluids expand as T ↑ or P ↓
• Fluids contract as T ↓ or P ↑
• What flow properties do we need to relate volume
changes to changes in P and T?
– Coefficient of Compressibility
T T
P Pv
v
//
P
VV
Pk
For water k = 2.2 GPa,
1 MPa pressure change = 0.05%
volume change
Water is relatively incompressible In term of finite changes:
Example 2-3
• Given: Pressure of 2 MPa is
applied to a mass of water that
initially filled 1000-cm3 volume.
Take a K = 5x 109 Pa
• Find: Volume after the pressure is
applied.
• Solution:
3
3
3
9
6
600.999
400.01000
400.0
1000105
102
/
cmV
VVV
cm
cmPax
Pax
VK
pV
VV
pK
final
final
Coefficient of Compressibility
• What flow properties do we need to relate volume
changes to changes in P and T?
– Coefficient of Compressibility
– Coefficient of volume expansion
– Combined effects of P and T can be written as
1 1
P P
v
v T T
P T
v vdv dT dP
T P
In term of finite changes:
TT
VVB
// (at P constant)
Viscosity
• Viscosity of a fluid is measure of its resistance to motion. The tangential force per unit area is called shear stress, and is expressed for simple shear flow between plates (1D) as:
• Drag force is the force a flowing
fluid exerts on a body in the flow
direction. The magnitude of this
force depends, in part, on
viscosity
dy
du
Viscosity Newtonian fluids: Fluids for
which the rate of deformation
is proportional to the shear
stress.
Shear
stress
Shear force
coefficient of viscosity
Dynamic (absolute) viscosity
kg/m s or N s/m2 or Pa s
1 poise = 0.1 Pa s
The behavior of a fluid in laminar flow between two
parallel plates when the upper plate moves with a constant
velocity.
Viscosity
The rate of deformation (velocity gradient) of a
Newtonian fluid is proportional to shear stress, and
the constant of proportionality is the viscosity.
Variation of shear stress with the rate of
deformation for Newtonian and non-Newtonian
fluids (the slope of a curve at a point is the
apparent viscosity of the fluid at that point).
Kinematic Viscosity
m2/s or stoke
1 stoke = 1 cm2/s
Dynamic viscosity, in general,
does not depend on pressure, but
kinematic viscosity does.
For gases:
For liquids
Surface Tension
• Liquid droplets behave like small balloons
filled with the liquid on a solid surface, and the
surface of the liquid acts like a stretched elastic
membrane under tension.
• The pulling force that causes this tension acts
parallel to the surface and is due to the
attractive forces between the molecules of the
liquid.
• The magnitude of this force per unit length is
called surface tension (or coefficient of surface
tension) and is usually expressed in the unit
N/m.
• This effect is also called surface energy [per
unit area] and is expressed in the equivalent
unit of N m/m2.
Attractive forces acting on a liquid molecule at the
surface and deep inside the liquid.
Surface Tension
Stretching a liquid film with a U-shaped
wire, and the forces acting on the movable
wire of length b.
W = The work done during this stretching process
Capillary Effects
Capillary effect: The rise or fall of a liquid in a small-diameter tube inserted
into the liquid.
Capillaries: Such narrow tubes or confined flow channels.
The capillary effect is partially responsible for the rise of water to the top of tall
trees.
Meniscus: The curved free surface of a liquid in a capillary tube.
The contact angle for wetting and
nonwetting fluids.