Thermodynamics 10302020 CIDERITP Summer School How does Earth

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Thermodynamics 10/30/2020 CIDER/ITP Summer School

Thermodynamics 10/30/2020 CIDER/ITP Summer School

How does Earth respond? • To changes in energy – Change in temperature (Heat

How does Earth respond? • To changes in energy – Change in temperature (Heat Capacity) – Change in Density (thermal expansivity – Phase Transformations (Gibbs free energy) • To hydrostatic stress – Compression (bulk modulus) – Adiabatic heating (Grüneisen parameter) • To deviatoric stress – Elastic deformation (elastic constants) – Flow (viscosity) – Failure (state and rate dependent friction) • Rates of Transport of – – Mass (chemical diffusivity) Energy (thermal diffusivity) Momentum (viscosity, attenuation) Charge (electrical conductivity)

Mantle Phases Wadsleyite (wa); Ringwoodite (ri); akimotoite (ak); Mg-perovskite (mgpv); Ca-perovskite (capv); Ferropericlase (fp)

Mantle Phases Wadsleyite (wa); Ringwoodite (ri); akimotoite (ak); Mg-perovskite (mgpv); Ca-perovskite (capv); Ferropericlase (fp)

Scope of Thermodynamics • Applicable to any system • Only to a certain set

Scope of Thermodynamics • Applicable to any system • Only to a certain set of states, called equlibrium states • Only to certain properties of those states: macroscopic • No specific, quantitative predictions, instead, limits and relationships

Equilibrium Spinel Peridotite P(1), T(1), Ni(1)=Ni(2)=Ni(f) Perovskitite P(2), T(2), Ni(2) Garnet Peridotite P(f), T(f),

Equilibrium Spinel Peridotite P(1), T(1), Ni(1)=Ni(2)=Ni(f) Perovskitite P(2), T(2), Ni(2) Garnet Peridotite P(f), T(f), Ni(f)

Macroscopic Properties • • Volume (Density) Entropy Energy Proportions of Phases Composition of Phases

Macroscopic Properties • • Volume (Density) Entropy Energy Proportions of Phases Composition of Phases … Not – Crystal size – Crystal shape – Details of arrangement

Thermodynamic Variables • Second Order – Heat capacity – Thermal expansivity – Bulk modulus

Thermodynamic Variables • Second Order – Heat capacity – Thermal expansivity – Bulk modulus – Grüneisen parameter • First Order – – – V: Volume, S: Entropy Ni: Amount of components P: Pressure T: Temperature I : Chemical Potential

Foundations 1 H. B. Callen, Thermodynamics and an Introduction to Thermostatistics, 2 ed, Wiley,

Foundations 1 H. B. Callen, Thermodynamics and an Introduction to Thermostatistics, 2 ed, Wiley, 1985 • What defines the equilibrium state of our system? – Three quantities • Ni (Composition) • V (Geometry) • U (potential and kinetic) • Ideal Gas – Energy is all kinetic so – U = i mivi 2 – ways to redistribute KE among particles while leaving U unchanged

Foundations 2 • Entropy – S = Rln – S = S(U, V, Ni)

Foundations 2 • Entropy – S = Rln – S = S(U, V, Ni) • Relationship to U – As U decreases, S decreases – S monotonic, continuous, differentiable: invertible • U = U(S, V, Ni) • Fundamental Thermodynamic Relation

Properties of Internal Energy, U • Complete First Law

Properties of Internal Energy, U • Complete First Law

Fundamental Relation • U = U(S, V, Ni) • Complete information of all properties

Fundamental Relation • U = U(S, V, Ni) • Complete information of all properties of all equilibrium states • S, V, Ni are natural variables of U • U = U(T, V, Ni) not fundamental

Legendre Transformations y • Two equivalent representations – y=f(x) – =y-px – i. e.

Legendre Transformations y • Two equivalent representations – y=f(x) – =y-px – i. e. =g(p) • Identify – y U, x V, S, p P, T, G • G = U - d. U/d. V V - d. U/d. S S or • G(P, T, Ni) = U(V, S, Ni) + PV - TS • G(P, T, Ni) is also fundamental! x

Fundamental thermodynamic relation H. B. Callen, Thermodynamics, Wiley, 1965, 1985. Steam Tables All thermodynamic

Fundamental thermodynamic relation H. B. Callen, Thermodynamics, Wiley, 1965, 1985. Steam Tables All thermodynamic properties of water and steam at all P, T Density, thermal expansivity, compressibility, heat capacity, entropy, saturation, enthalpy, … pg. 1: F(V, T) pp. 2 -320: V and T derivatives of F

Thermodynamic Square • Thermodynamic Potentials – – F = Helmholtz free energy G =

Thermodynamic Square • Thermodynamic Potentials – – F = Helmholtz free energy G = Gibbs free energy H = Enthalpy U = Internal energy V F U S • Surrounded by natural variables • First derivatives • Second derivatives (Maxwell Relations) T G H P

Summary of Properties

Summary of Properties

Phase Equilibria • How does G change in a spontaneous process at constant P/T?

Phase Equilibria • How does G change in a spontaneous process at constant P/T? – – – L 1: d. U = d. Q - Pd. V L 2: d. Q ≤ Td. S d. G = d. U + Pd. V + vd. P - Td. S - Sd. T Substitute L 1, take constant P, T d. G = d. Q - Td. S This is always less than zero by L 2. • G is lowered by any spontaneous process • State with the lowest G is stable

One Component Phase Equilibria d. G = Vd. P - Sd. T G G

One Component Phase Equilibria d. G = Vd. P - Sd. T G G A Slope=-S B Slope=V Ptr P Phase Diagram T Ttr B A P T

Two Component Phase Equilibria • Phase: Homogeneous in chemical composition and physical state •

Two Component Phase Equilibria • Phase: Homogeneous in chemical composition and physical state • Component: Chemically independent constituent • Example: (Mg, Fe)2 Si. O 4 • Phases: olivine, wadsleyite, ringwoodite, … • Components: Mg 2 Si. O 4, Fe 2 Si. O 4 • Why not Mg, Fe, Si, O?

Phase Rule • p phases, c components • Equilibrium: uniformity of intensive variables across

Phase Rule • p phases, c components • Equilibrium: uniformity of intensive variables across coexisting phases: • P(a), T(a), i(a) • Equations – 2(p-1)+c(p-1) • Unknowns – 2 p+p(c-1) • Degrees of Freedom – f=c-p+2 c≈5, p≈4 f≈3

Properties of ideal solution 1 – N 1 type 1 atoms, N 2 type

Properties of ideal solution 1 – N 1 type 1 atoms, N 2 type 2 atoms, N total atoms – x 1=N 1/N, x 2=N 2/N • Volume, Internal energy: linear – V = x 1 V 1 + x 2 V 2 • Entropy: non-linear – S = x 1 S 1 + x 2 S 2 -R(x 1 lnx 1 + x 2 lnx 2) • Sconf = Rln – is number of possible of arrangements.

Properties of Ideal Solution 2 • Gibbs free energy – G = x 1

Properties of Ideal Solution 2 • Gibbs free energy – G = x 1 G 1 + x 2 G 2 + RT(x 1 lnx 1 + x 2 lnx 2) • Re-arrange – G = x 1(G 1 + RTlnx 1) + x 2(G 2 + RTlnx 2) • G = x 1 1 + x 2 2 • i = Gi + RTlnxi

Non-ideal solutions • Internal Energy a non-linear function of composition – Compare A-B bond

Non-ideal solutions • Internal Energy a non-linear function of composition – Compare A-B bond energy to average of A-A, B-B – Tendency towards dispersal, clustering. • Exsolution – cpx-opx, Mg-pv, Ca-pv • Formally: – I = Gi + RTlnai – ai is the activity and may differ from the mole fraction

Example: Thermochemistry • Increase temperature slightly, measure heat evolved • CP=(d. H/d. T)P •

Example: Thermochemistry • Increase temperature slightly, measure heat evolved • CP=(d. H/d. T)P • CV 3 R • Calculate S, H by integration • (d. T/d. P)eq= V/ S • Debye Model Stixrude and Lithgow-Bertelloni (2005)

Equation of State • Start from fundamental relation • Helmholtz free energy – F=F(V,

Equation of State • Start from fundamental relation • Helmholtz free energy – F=F(V, T, Ni) • Isotherm, fixed composition – F=F(V) • Taylor series expansion • Expansion variable must be V or function of V – F = af 2 + bf 3 + … • f = f(V) Eulerian finite strain • a = 9 K 0 V 0

Grüneisen Parameter • Thermal pressure • Adiabatic Gradient • Dimensionless • 1 -2 for

Grüneisen Parameter • Thermal pressure • Adiabatic Gradient • Dimensionless • 1 -2 for most mantle phases • Decreases on compression Note: =1/V=density

Thermal pressure Thermal expansion

Thermal pressure Thermal expansion