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Arthur Holmes (1945)

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Arthur Holmes (1945). ?. Various Conceptual Models (i.e., hypotheses) of Large-Scale Mantle Convection Inspired by Seismology and/or geochemistry. - PowerPoint PPT Presentation

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Page 1: Arthur Holmes  (1945)

Arthur Holmes (1945)

Page 2: Arthur Holmes  (1945)

Dziewonski et al. (2010)

Kellogg et al. (1999)

Courtillot et al. (2003)

Jellinek and Manga (2004) Garnero (web)

Various Conceptual Models (i.e., hypotheses) of Large-Scale Mantle Convection Inspired by Seismology and/or geochemistry. Each hypothesis has fundamentally different consequences for our understanding of mantle convection and how it cools the Earth and drives plate tectonics.

?

Page 3: Arthur Holmes  (1945)

Dziewonski et al. (2010)

Kellogg et al. (1999)

Courtillot et al. (2003)

Jellinek and Manga (2004) Garnero (web)

?Discovering which, if any, of these are occurring in the Earth is critical toward building the foundation for our understanding of:

Driving forces of mantle convection and plate tectonics (e.g., slab-driven versus superplume-driven convection) Heat transport and thermal evolution Chemical evolution and MORB/OIB chemistry. The geodynamo Hotspots and the morphology, size, temperature, and the chemistry of plumes.

Page 4: Arthur Holmes  (1945)

Geodynamics of Mantle Convection

Physics (Conservations of mass, momentum, and energy)

Application/Modeling (Numerical modeling, laboratory experiments)

Science (Observations, hypothesis development, hypothesis testing)

Page 5: Arthur Holmes  (1945)

Independent Variables:

t = timex, y, z = position

Dependent Variables:

Conservation of Mass

Rate of mass change in a volume

Rate of mass entering the volume

Rate of mass exiting the volume

= -

Vt

tzyx ,,,

),,,( tzyxV

Density (scalar field)

Velocity (vector field)

VVt

This is identical to:

Page 6: Arthur Holmes  (1945)

Conservation of Momentum

Rate of momentum change per volume

Rate of momentum entering the volume

Rate of momentum exiting the volume

= - Force acting on the volume

+

Page 7: Arthur Holmes  (1945)

Independent Variables:

t = timex, y, z = position

Dependent Variables:

Conservation of Momentum

tzyx ,,,

),,,( tzyxV

Density (scalar field)

Velocity (vector field)

gVVtV

tzyx ,,,

tzyxg ,,,

Stress (tensor field)

Gravitational acceleration (vector field)

Derivation includes using conservation of mass.

Page 8: Arthur Holmes  (1945)

Image from http://homepage.ufp.pt/biblioteca/GlossarySaltTectonics/Pages/PageS.html

ab

Stress

“a” is the normal to the plane that the stress acts upon

“b” is the direction of the stress

NOTE: 1, 2, 3 are the same as x, y, z

Page 9: Arthur Holmes  (1945)

It is often convenient to decompose the stress tensor into 2 parts:

1. Pressure, p (scalar)

2. Deviatoric Stress, (tensor field)

Pressure is defined to be the average of normal stresses:

zzyyxxp 31

Image from http://www.see.ed.ac.uk/~johnc/teaching/fluidmechanics4/2003-04/fluids5/stress.html

Pressure acts only in the normal direction.Pressure is the same in each direction.By convention, pressure is in the opposite direction of stress direction.

Page 10: Arthur Holmes  (1945)

By construction:

zzyyxxp 31

Ip

Therefore, the deviatoric stress is defined as:

100010001

I

Note that:

Ip

Important note: directions for stress, deviatoric stress, and pressure are not a universal convention, so be careful!

Page 11: Arthur Holmes  (1945)

Let’s look at the following term in the momentum equation:

p

kzpj

ypi

xp

pp

pk

zj

yi

x

Ip

Ip

ˆˆˆ

000000

ˆ,ˆ,ˆ

Page 12: Arthur Holmes  (1945)

Independent Variables:

t = timex, y, z = position

Dependent Variables:

Conservation of Momentum (different form, with pressure)

tzyx ,,,

),,,( tzyxV

Density (scalar)

Velocity (vector field)

gpVVtV

tzyx ,,,

tzyxg ,,,

Deviatoric stress (tensor field)

Gravitational acceleration (vector field)

tzyxp ,,, Pressure (scalar)

Page 13: Arthur Holmes  (1945)

Conservation of Energy

Rate of internal energy change in a volume

Rate of heat transferred to the volume

Rate of heat exiting the volume

= _Rate of work performed by the volume

_

This is the time derivative of the first law of thermodynamics.

WQdU

Page 14: Arthur Holmes  (1945)

Independent Variables (x,y,z,t)

Dependent Variables:

Conservation of Energy

tzyx ,,,

),,,( tzyxV

Density (scalar field)

Velocity (vector field)

DtDSV

DtDpTTkTVc

tTc pp

*:

tzyx ,,,

*dS

Deviatoric stress (tensor field)

Entropy changes related to processes other than those for a homogenous material undergoing changes in temperature and pressure.

Derivation includes using conservation of mass, conservation of momentum, and dU = TdS – PdV (1st and 2nd laws of thermo).

tzyxk ,,, Thermal conductivity (scalar field)

PTV

V

1 Thermal expansivity [V is volume] (scalar field)

TTSC

PP

Specific heat at constant pressure (scalar field)

tzyxT ,,, Temperature (scalar field)

Page 15: Arthur Holmes  (1945)

Some Explanation:

During the derivation, entropy changes were split into 2 types:

1. Entropy changes due to single phase, homogeneous material undergoing changes in temperature and pressure.

2. All other entropy changes are lumped into: S* These include things such as radioactive heat production, phase changes, chemical reactions, nuclear reactions, etc. These items are best extracted as needed for the particular problem at hand. Radioactive heat production of uranium, thorium, and potassium is often extracted as: H

Page 16: Arthur Holmes  (1945)

Independent Variables (x,y,z,t)

Dependent Variables:

Conservation of Energy (with heat production explicitly defined)

tzyx ,,,

),,,( tzyxV

Density (scalar field)

Velocity (vector field)

DtDSHV

DtDpTTkTVc

tTc pp

*:

tzyx ,,,

*dS

Deviatoric stress (tensor field)

Entropy changes related to “extra” processes

Derivation includes using conservation of mass, conservation of momentum, and dU = TdS – PdV (1st and 2nd laws of thermo).

tzyxk ,,, Thermal conductivity (scalar field)

PTV

V

1 Thermal expansivity [V is volume] (scalar field)

TTSC

PP

Specific heat at constant pressure (scalar field)

tzyxT ,,, Temperature (scalar field)

tzyxH ,,, Heat production (power per mass)

Page 17: Arthur Holmes  (1945)

Some Explanation on Notation:

V

: This is a scalar, defined by:j

iij

ij xV

3

1

3

1

This term describes the heat produced by friction, and is often called the “viscous dissipation.”

Page 18: Arthur Holmes  (1945)

Some Explanation on Notation:

DtD

Is called the “material derivative,” and it is defined as:

VtDt

D

TVtT

DtDT

The material derivative can act on a scalar or a vector. For example:

VVtV

DtVD

Page 19: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Mass

Momentum

Energy

Summary: Conservation Equations (No approximations)

Page 20: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Inertia term. Material remains in constant motion unless acted upon by forces on the R.H.S.

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 21: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Pressure term: material typically flows from high to low pressure.

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 22: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Stress term: viscous and elastic processes that transfer stress.

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 23: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Buoyancy term: the weight of the volume.

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 24: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Conduction term: heat diffuses from hot to cold

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 25: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Adiabatic term: rising material expands and cools, vice versa.

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 26: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Viscous dissipation term: viscous friction generates heat.

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 27: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Heat production term: can be prescribed as needed.

Summary: Conservation Equations (No approximations)

Mass

Momentum

Energy

Page 28: Arthur Holmes  (1945)

Vt

gpDtVD

DtDSHV

DtDpTTk

DtDTcp

*:

Summary: Conservation Equations (No approximations)

Additional entropy changes: can be prescribed as needed.

Mass

Momentum

Energy

Page 29: Arthur Holmes  (1945)

We haven’t made any approximations thus far.

Now, we’ll work toward transforming these equations into the forms that we typically use in modeling.

This involves 3 things:

1. Definition of a reference model.

2. Non-dimensionalization of variables

3. Approximations of physics and material parameters.

Page 30: Arthur Holmes  (1945)

Reference ModelIf the dynamics are largely driven by perturbations to a stable reference state, then it often becomes convenient to decompose some variables into 2 parts, a reference part and a perturbation part.

Density:

tzyxzyxtzyx REF ,,,~,,,,,

Page 31: Arthur Holmes  (1945)

Pressure:

tzyxpzyxptzyxp REF ,,,~,,,,,

Gravitational acceleration:

tzyxgzyxgtzyxg REF ,,,~,,,,,

Temperature:

tzyxTzyxTtzyxT REF ,,,~,,,,,

p~Note: The perturbation for pressure is given the name: dynamic pressure

Page 32: Arthur Holmes  (1945)

In our reference model, the reference pressure should be a self-consistent hydrostatic pressure due to the reference density and reference gravity.

REFREFREF gp

Page 33: Arthur Holmes  (1945)

Conservation of Mass:

Vt

Vtt

REF

~

Vt

~

Page 34: Arthur Holmes  (1945)

Conservation of Momentum:

ggppDtVD

REFREFREF~~~

~~~~ REFREFREFREFREF gggppDtVD

~~~~ REFREFREFREFREFREF gggpgDtVD

~~~~ REFREF ggpDtVD

Page 35: Arthur Holmes  (1945)

Conservation of Energy:

DtDSHV

DtDpTTk

DtDTcp

*:

DtDSHVpp

DtDTTk

DtDTc REFp

*:~

DtDSHVp

DtDTp

DtDTTk

DtDTc REFp

*:~

Page 36: Arthur Holmes  (1945)

REFREFREF pVpt

pDtD

REFREFREF gVpDtD

So

DtDSHVp

DtDTgVTTk

DtDTc REFREFp

*:~

Page 37: Arthur Holmes  (1945)

Summary: Conservation Equations, with reference model.(Still no approximations)

Mass

Momentum

Energy

~~~~ REFREF ggpDtVD

Vt

~

DtDSHVp

DtDTgVTTk

DtDTc REFREFp

*:~

Page 38: Arthur Holmes  (1945)

Non-dimensionalization of variables.

Why!?

1. To make the problem scalable. For example, we can model mantle convection in a fish tank, as long as we scale the parameters appropriately.

2. Leads to non-dimensional collection of variables that can be used to characterize the system. For example, Rayleigh number, Reynolds number, Dissipation number, Buoyancy number.

3. Allows for a better understanding of parameter trade-offs. For example, if you double both density and viscosity, the system remains unchanged. For example doubling density is equivalent to halving the viscosity.

4. Numbers are closer to unity. Allows better computational applicability.

Page 39: Arthur Holmes  (1945)

There are many ways to non-dimensionalize a system. The key is: we make the rules. Choose transformations that will be useful. For thermal convection problems, we can transform the following:

tzyxVh

tzyxV

tzyxTtzyxzyxzyx

tzyxtzyx

o

oo

REFoREF

o

,,,,,,

,,,~,,,~,,,,,,,,,,

Note: primed variables

are non-dimensional

Page 40: Arthur Holmes  (1945)

),,,(),,,(),,,(),,,(

,,,~,,,~,,,,

,,,,,,

,,,~,,,~

2

2

tzyxkCtzyxktzyxTTtzyxT

CCC

tzyxggtzyxg

zyxggzyxg

tzyxh

tzyx

tzyxph

tzyxp

opoo

popp

o

REFoREF

oo

oo

Page 41: Arthur Holmes  (1945)

DtD

hDtD

h

tht

tzyxHhTC

tzyxH

o

o

op

o

o

2

2

2

1

),,,(),,,(

Page 42: Arthur Holmes  (1945)

Summary: Non-dimensional Conservation Equations, with reference model. Primes have been dropped. (Still no approximations)

Mass

Momentum

~~

~~

3

3

Tghg

gThgpDtVD

oREFoo

oo

REFoo

ooo

o

oo

Vt

To

~

Page 43: Arthur Holmes  (1945)

Energy

HVpDtDT

hc

gVTc

hgTkDtDTc

op

o

REFREFp

oop

o

o

:~2

Page 44: Arthur Holmes  (1945)

We introduce the following collections of variables:

oo

o

p

oo

oo

ooo

oc

hgDi

ThgRa

Pr

3

Rayleigh number

Dissipation number

Prandtl number

Page 45: Arthur Holmes  (1945)

Summary: Non-dimensional Conservation Equations, with reference model. Primes have been dropped. (Still no approximations)

Mass

Momentum

~1~~~

Pr1

REFo

REF TgRagRap

DtVD

Vt

To

~

HVRaDip

DtDT

RaTDigVTDiTk

DtDTc o

REFREFp

:~

Energy

Page 46: Arthur Holmes  (1945)

Now, lets examine various approximations appropriate for mantle convection modeling:

Assumption: 0

~

t

Justification: This term is mainly relevant if the system has shock waves. Shock waves can be important if convection velocities are comparable to the speed of sound. Mantle convection velocities are much slower! cm/yr versus km/s.

0 V

Conservation of mass

This is called the anelastic liquid approximation (ALA)

Page 47: Arthur Holmes  (1945)

The Prandtl number is a measure of the viscous resistance to inertia.

oo

o

Pr

Viscous stresses act to resist continued motion. They diffuse momentum.

Imagine stirring a pot of honey and a pot of water. When you stop stirring, the water will continue to flow, but the honey will stop.

For Earth’s mantle:

3

26

20

4000~

10~

10~

mkgsm

sPa

o

o

o

2210~Pr

Therefore 1/Pr is close to zero!

Page 48: Arthur Holmes  (1945)

Assumption:

0Pr1

Justification: The Earth’s mantle has such a high viscosity that it requires constant forcing to continue to flow.

Conservation of momentum

This is called the infinite Prandtl number approximation

~1~~~

Pr1

REFo

REF TgRagRap

DtVD

0~1~~~

REF

oREF T

gRagRap

Page 49: Arthur Holmes  (1945)

Assumption: There are no perturbations to the reference gravitational acceleration. This term is usually only included if one wishes to include self-gravitation due to internal density heterogeneities and dynamic topography.

Conservation of momentum

0~1~~~

REF

oREF T

gRagRap

0~ g

0~~ REFgRap

Page 50: Arthur Holmes  (1945)

Summary: Non-dimensional Conservation Equations, with reference model. Primes have been dropped. Approximations: anelastic liquid (ALA), infinite Prandtl number, static gravitational field.

Mass

Momentum

Energy

0 V

0~~ REFgRap

HVRaDip

DtDT

RaTDigVTDiTk

DtDTc o

REFREFp

:~

Page 51: Arthur Holmes  (1945)

Assumption: Truncated Liquid Anelastic Liquid Approximation (TALA)

Dynamic pressure does not contribute to density perturbations:

tzyxptzyxCtzyxT ,,,~),,,,(,,,,~

The material derivative of dynamic pressure is negligible. 0~ pDtD

HVRaDip

DtDT

RaTDigVTDiTk

DtDTc o

REFREFp

:~

Page 52: Arthur Holmes  (1945)

Summary: Non-dimensional Conservation Equations, with reference model. Primes have been dropped. Approximations: truncated anelastic liquid (TALA), infinite Prandtl number, static gravitational field.

Mass

Momentum

Energy

0 V

0~~ REFgRap

HVRaDigVTDiTk

DtDTc REFREFp

:

Page 53: Arthur Holmes  (1945)

Approximation: Extended Boussinesq Approximation (EBA)

Density is constant, ρo, except for density perturbations in the momentum equation.

0,,~

1,,

zyx

zyxREF

Except for in the momentum equation

The main consequence of this approximation is that makes the fluid incompressible:

0 V

Page 54: Arthur Holmes  (1945)

Summary: Non-dimensional Conservation Equations, with reference model. Primes have been dropped. Approximations: Extended Boussinesq Approximation (EBA), infinite Prandtl number, static gravitational field.

Mass

Momentum

Energy

0 V

0~~ REFgRap

HVRaDigVTDiTk

DtDTc REFp

:

Page 55: Arthur Holmes  (1945)

Approximation: Boussinesq Approximation (BA)

Neglect all terms that include the Dissipation number (viscous dissipation, adiabatic heating/cooling). Specific heat, thermal expansivity, and thermal conductivity is constant.

Page 56: Arthur Holmes  (1945)

Summary: Non-dimensional Conservation Equations, with reference model. Primes have been dropped. Approximations: Boussinesq Approximation (BA), infinite Prandtl number, static gravitational field.

Mass

Momentum

Energy

0 V

0~~ REFgRap

HTDtDT

2

Page 57: Arthur Holmes  (1945)

The stress and density perturbation terms are prescribed for the particular problem at hand.

For mantle convection, the stress is usually assumed to be viscous and isotropic.

IVIVbulk

312

31

IV

312 (ALA and TALA)

2 (EBA and BA)

Page 58: Arthur Holmes  (1945)

KpTCtzyxptzyxCtzyxT REF

~~,,,~,,,,,,,,~

Dimensional density perturbation

(ALA)

TCtzyxCtzyxT REF~,,,,,,,~ (TALA)

TCtzyxCtzyxT o~,,,,,,,~ (EBA and BA)

Page 59: Arthur Holmes  (1945)
Page 60: Arthur Holmes  (1945)