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Mathematical Equations of CFD

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Title: Mathematical Equations of CFD


1
Mathematical Equations of CFD
2
Outline
  • Introduction
  • Navier-Stokes equations
  • Turbulence modeling
  • Incompressible Navier-Stokes equations
  • Buoyancy-driven flows
  • Euler equations
  • Discrete phase modeling
  • Multiple species modeling
  • Combustion modeling
  • Summary

3
Introduction
  • In CFD we wish to solve mathematical equations
    which govern fluid flow, heat transfer, and
    related phenomena for a given physical problem.
  • What equations are used in CFD?
  • Navier-Stokes equations
  • most general
  • can handle wide range of physics
  • Incompressible Navier-Stokes equations
  • assumes density is constant
  • energy equation is decoupled from continuity and
    momentum if properties are constant

4
Introduction (2)
  • Euler equations
  • neglect all viscous terms
  • reasonable approximation for high speed flows
    (thin boundary layers)
  • can use boundary layer equations to determine
    viscous effects
  • Other equations and models
  • Thermodynamics relations and equations of state
  • Turbulence modeling equations
  • Discrete phase equations for particles
  • Multiple species modeling
  • Chemical reaction equations (finite rate, PDF)
  • We will examine these equations in this lecture

5
Navier-Stokes Equations
Conservation of Mass
Conservation of Momentum
6
Navier-Stokes Equations (2)
Conservation of Energy
Equation of State
Property Relations
7
Navier-Stokes Equations (3)
  • Navier-Stokes equations provide the most general
    model of single-phase fluid flow/heat transfer
    phenomena.
  • Five equations for five unknowns r, p, u, v, w.
  • Most costly to use because it contains the most
    terms.
  • Requires a turbulence model in order to solve
    turbulent flows for practical engineering
    geometries.

8
Turbulence Modeling
  • Turbulence is a state of flow characterized by
    chaotic, tangled fluid motion.
  • Turbulence is an inherently unsteady phenomenon.
  • The Navier-Stokes equations can be used to
    predict turbulent flows but
  • the time and space scales of turbulence are very
    tiny as compared to the flow domain!
  • scale of smallest turbulent eddies are about a
    thousand times smaller than the scale of the flow
    domain.
  • if 10 points are needed to resolve a turbulent
    eddy, then about 100,000 points are need to
    resolve just one cubic centimeter of space!
  • solving unsteady flows with large numbers of grid
    points is a time-consuming task

9
Turbulence Modeling (2)
  • Conclusion Direct simulation of turbulence using
    the Navier-Stokes equations is impractical at the
    present time.
  • Q How do we deal with turbulence in CFD?
  • A Turbulence Modeling
  • Time-average the Navier-Stokes equations to
    remove the high-frequency unsteady component of
    the turbulent fluid motion.
  • Model the extra terms resulting from the
    time-averaging process using empirically-based
    turbulence models.
  • The topic of turbulence modeling will be dealt
    with in a subsequent lecture.

10
Incompressible Navier-Stokes Equations
Conservation of Mass
Conservation of Momentum
11
Incompressible Navier-Stokes Equations (2)
  • Simplied form of the Navier-Stokes equations
    which assume
  • incompressible flow
  • constant properties
  • For isothermal flows, we have four unknowns p,
    u, v, w.
  • Energy equation is decoupled from the flow
    equations in this case.
  • Can be solved separately from the flow equations.
  • Can be used for flows of liquids and gases at low
    Mach number.
  • Still require a turbulence model for turbulent
    flows.

12
Buoyancy-Driven Flows
  • A useful model of buoyancy-driven (natural
    convection) flows employs the incompressible
    Navier-Stokes equations with the following body
    force term added to the y momentum equation
  • This is known as the Boussinesq model.
  • It assumes that the temperature variations are
    only significant in the buoyancy term in the
    momentum equation (density is essentially
    constant).

b
thermal expansion coefficient
roTo
reference density and temperature
g gravitational acceleration (assumed pointing
in -y direction)
13
Euler Equations
  • Neglecting all viscous terms in the Navier-Stokes
    equations yields the Euler equations

14
Euler Equations (2)
  • No transport properties (viscosity or thermal
    conductivity) are needed.
  • Momentum and energy equations are greatly
    simplified.
  • But we still have five unknowns r, p, u, v, w.
  • The Euler equations provide a reasonable model of
    compressible fluid flows at high speeds (where
    viscous effects are confined to narrow zones near
    wall boundaries).

15
Discrete Phase Modeling
  • We can simulate secondary phases in the flows
    (either liquid or solid) using a discrete phase
    model.
  • This model is applicable to relatively low
    particle volume fractions (lt 10-12 by
    volume)
  • Model individual particles by constructing a
    force balance on the moving particle

Drag Force
Particle path
Body Force
16
Discrete Phase Modeling (2)
  • Assuming the particle is spherical (diameter D),
    its trajectory is governed by

17
Discrete Phase Modeling (3)
  • Can incorporate other effects in discrete phase
    model
  • droplet vaporization
  • droplet boiling
  • particle heating/cooling and combustion
  • devolatilization
  • Applications of discrete phase modeling
  • sprays
  • coal and liquid fuel combustion
  • particle laden flows (sand particles in an air
    stream)

18
Multiple Species Modeling
  • If more than one species is present in the flow,
    we must solve species conservation equations of
    the following form
  • Species can be inert or reacting
  • Has many applications (combustion modeling, fluid
    mixing, etc.).

19
Combustion modeling
  • If chemical reactions are occurring, we can
    predict the creation/depletion of species mass
    and the associated energy transfers using a
    combustion model.
  • Some common models include
  • Finite rate kinetics model
  • applicable to non-premixed, partially, and
    premixed combustion
  • relatively simple and intuitive and is widely
    used
  • requires knowledge of reaction mechanisms, rate
    constants (introduces uncertainty)
  • PDF model
  • solves transport equation for mixture fraction of
    fuel/oxidizer system
  • rigorously accounts for turbulence-chemistry
    interactions
  • can only include single fuel/single oxidizer
  • not applicable to premixed systems

20
Summary
  • General purpose solvers (such as those marketed
    by Fluent Inc.) solve the Navier-Stokes
    equations.
  • Simplified forms of the governing equations can
    be employed in a general purpose solver by simply
    removing appropriate terms
  • Example The Euler equations can be used in a
    general purpose solver by simply zeroing out the
    viscous terms in the Navier-Stokes equations
  • Other equations can be solved to supplement the
    Navier-Stokes equations (discrete phase model,
    multiple species, combustion, etc.).
  • Factors determining which equation form to use
  • Modeling - are the simpler forms appropriate for
    the physical situation?
  • Cost - Euler equations are much cheaper to solver
    than the Navier-Stoke equations
  • Time - Simpler flow models can be solved much
    more rapidly than more complex ones.
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