Presentation Slides for Chapter 3 of Fundamentals of Atmospheric Modeling 2 nd Edition Mark Z. Jacobson Department of Civil & Environmental Engineering.

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Presentation transcript:

Presentation Slides for Chapter 3 of Fundamentals of Atmospheric Modeling 2 nd Edition Mark Z. Jacobson Department of Civil & Environmental Engineering Stanford University Stanford, CA March 10, 2005

Velocity Rate at which the position of a body changes with time Wind Speed and Velocity Velocity vector (3.1) i,j,k= unit vectors in x-, y-, and z-directions Horizontal velocity vector (3.1) Scalar components of velocity (3.2)

Wind speed Magnitude of velocity vector (3.3) Wind Speed Horizontal wind speed (3.3)

Fig. 3.1 Zonally-Averaged Velocities Altitude (km) JanuaryJuly

Expand total derivative with chain rule (3.4) Local and Total Differentiation Total derivative. Time rate of change along trajectory Local derivative. Time rate of change at a fixed point Advection term. Time rate of change due to advection

Eulerian frame of reference Frame of reference of a point fixed in space Eulerian vs. Lagrangian Lagrangian frame of reference Frame of reference of moving parcel

Assume balloon traveling with the wind from east to west dN/dt = 10 8 molec. cm -3 s -1 ∂N/∂x = molec. cm -3 km -1 u= -10 m s -1 Find time-rate-of-change in concentration at fixed point Example 3.1

Gradient operator in Cartesian-altitude coordinates (3.6) Gradient Operator Dot product of velocity vector with gradient operator (3.7)

Dot product of gradient operator with velocity vector (3.8) Divergence term Gradient Operator Dot product of gradient operator with velocity vector not symmetric Dot product of two vectors is symmetric

Product of concentration and divergence term is scalar (3.9) Gradient Operator Gradient of a scalar is a vector (3.10) Advection term is a scalar (3.11)

Total derivative of scalar concentration (3.12) Gradient Operator Advection term (3.11) Generalized and expanded form of total derivative (3.13)

Scalar Continuity Equation Accumulation = inflow minus outflow (3.14)

Scalar Continuity Equation Accumulation = inflow minus outflow (3.14) Divide both sides by  t and box volume (  x  y  z) (3.15) Let  t,  x-->0 (3.16) Flux-divergence form of continuity equation

Scalar Continuity Equation Flux-divergence form of continuity equation in 3-D (3.17) --> Velocity divergence continuity equation (and for air) (3.22,3) Expand with chain rule (3.18) From definition of total derivative (3.21) Substitute (3.21) into (3.18)

Mixing Ratio Continuity Equation Number conc. as function of moist-air mixing ratio (3.24) to obtain (3.25) Substitute into continuity equation for number conc. (3.19) Note that --> Continuity equation for moist-air mass mixing ratio (3.26)

Compressible/Incompressible Compressible fluid Volume of an air or water parcel changes over time Density of incompressible fluid constant along motion (3.28) Density of incompressible fluid changes at fixed point (3.29) Incompressible fluid (3.27) Volume of an air or water parcel is constant over time

Expanded Continuity Equation Expanded continuity equation(3.30) to obtain (3.32) Substitute (3.31)

Reynolds Averaging Precise gas concentration(3.33) Fig Precise, mean, and perturbation components of scalar velocity and number concentration Time- and grid-volume average concentration(3.34)

Expanded Continuity Equation Expanded continuity equation(3.32) Substitute precise concentrations and velocities and eliminate zero terms (3.40)

Expanded Continuity Equation Turbulent diffusion >> molecular diffusion -->(3.41) Number conc. continuity equation in vector notation (3.42) Continuity equation for air in vector notation (3.43)

Mixing Ratio Continuity Equation Moist-air mass mixing ratio continuity equation(3.44) Continuity equation for air (3.20) Sum continuity equations (3.45) Continuity equation after Reynolds averaging (3.49)

K-theory Relates turbulent fluxes of one parameter to the gradient of the mean value of the parameter Kinematic turbulent flux terms (3.50) K= eddy diffusion coefficient for energy (cm 2 s -1 ) Substitute into continuity equation (3.49)

Gas Continuity Equation Continuity equation for gas concentration(3.52) Continuity equation for moist-air mass mixing ratio (3.54) Eddy diffusion tensor (3.53)

Continuity Equations Continuity equation for air(3.55) Ignore turbulent flux divergence and external source/sink terms Expanded continuity equation for gas concentration (3.56)

Particle Continuity Equation Continuity equation for particle number concentration(3.58) Volume concentration (3.57) Continuity equation for particle volume concentration (3.59)

Water Continuity Equation Continuity equation for water vapor(3.61) Continuity equation for liquid water (3.62) Continuity equation for ice (3.63)

Bulk vs. Size-Resolved Size-resolved treatment of water(3.60) Bulk treatment of water

Thermodynamic Energy Equation First law of thermodynamics(2.82) Differentiate with respect to time, substitute  a =1/  a (3.64) Thermodynamic energy equation in terms of temperature along line of motion of parcel Time-rate-of change of temperature in a parcel is affected by diabatic sources/sinks and adiabatic expansion/contraction

Thermodynamic Energy Equation Differentiate  v =T v (1000 hPa/p a )  (3.65) Thermodynamic energy equation (3.64) Substitute dT v /dt from (3.65) into (3.64) (3.66)

Thermodynamic Energy Equation Sum the result(3.67) Substitute into (3.67) (3.73) Define energy density (J m -3 )

Thermodynamic Energy Equation Decompose variables (assume  ’ a small)(3.60) Perform Reynolds averaging (3.70) Thermodynamic energy equation Turbulent flux divergence terms (3.73)

Thermodynamic Energy Equation Turbulent flux divergence tensor(3.60) Expand diabatic source/sink term (3.75,6) Thermodynamic energy equation turbulence tensor(3.74)