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Onsager reciprocal relations

From Wikipedia, the free encyclopedia
Relations between flows and forces, or gradients, in thermodynamic systems
"Fourth law of thermodynamics" redirects here. For the fourth principle of energetics proposed by H. T. Odum, seeMaximum power principle. For the economic principle proposed by Nicholas Georgescu-Roegen, seeNicholas Georgescu-Roegen § Controversies.
Thermodynamics
The classicalCarnot heat engine

Inthermodynamics, theOnsager reciprocal relations express the equality of certain ratios betweenflows andforces inthermodynamic systems out ofequilibrium, but where a notion oflocal equilibrium exists.

"Reciprocal relations" occur between different pairs of forces and flows in a variety of physical systems. For example, consider fluid systems described in terms of temperature, matter density, and pressure. In this class of systems, it is known thattemperature differences lead toheat flows from the warmer to the colder parts of the system; similarly,pressure differences will lead tomatter flow from high-pressure to low-pressure regions. What is remarkable is the observation that, when both pressure and temperature vary, temperature differences at constant pressure can cause matter flow (as inconvection) and pressure differences at constant temperature can cause heat flow. Perhaps surprisingly, the heat flow per unit of pressure difference and thedensity (matter) flow per unit of temperature difference are equal. This equality was shown to be necessary byLars Onsager usingstatistical mechanics as a consequence of thetime reversibility of microscopic dynamics (microscopic reversibility). The theory developed by Onsager is much more general than this example and capable of treating more than two thermodynamic forces at once, with the limitation that "the principle of dynamical reversibility does not apply when (external) magnetic fields orCoriolis forces are present", in which case "the reciprocal relations break down".[1]

Though the fluid system is perhaps described most intuitively, the high precision of electrical measurements makes experimental realisations of Onsager's reciprocity easier in systems involving electrical phenomena. In fact, Onsager's 1931 paper[1] refers tothermoelectricity and transport phenomena inelectrolytes as well known from the 19th century, including "quasi-thermodynamic" theories byThomson andHelmholtz respectively. Onsager's reciprocity in the thermoelectric effect manifests itself in the equality of the Peltier (heat flow caused by a voltage difference) and Seebeck (electric current caused by a temperature difference) coefficients of a thermoelectric material. Similarly, the so-called "directpiezoelectric" (electric current produced by mechanical stress) and "reverse piezoelectric" (deformation produced by a voltage difference) coefficients are equal. For many kinetic systems, like theBoltzmann equation orchemical kinetics, the Onsager relations are closely connected to the principle ofdetailed balance[1] and follow from them in the linear approximation near equilibrium.

Experimental verifications of the Onsager reciprocal relations were collected and analyzed by D. G. Miller[2] for many classes of irreversible processes, namely forthermoelectricity,electrokinetics, transference inelectrolyticsolutions,diffusion,conduction of heat andelectricity inanisotropicsolids,thermomagnetism andgalvanomagnetism. In this classical review,chemical reactions are considered as "cases with meager" and inconclusive evidence. Further theoretical analysis and experiments support the reciprocal relations for chemical kinetics with transport.[3]Kirchhoff's law of thermal radiation is another special case of the Onsager reciprocal relations applied to the wavelength-specific radiativeemission andabsorption by a material body inthermodynamic equilibrium.

For his discovery of these reciprocal relations,Lars Onsager was awarded the 1968Nobel Prize in Chemistry. The presentation speech referred to the three laws of thermodynamics and then added "It can be said that Onsager's reciprocal relations represent a further law making a thermodynamic study of irreversible processes possible."[4] Some authors have even described Onsager's relations as the "Fourth law of thermodynamics".[5]

Classical cross effects
Potential \ FluxHeatElectricDiffusionDeformation
TemperatureThermal conductionSeebeck effectSoret effect (thermophoresis)Thermal expansion
VoltagePeltier effectOhm's lawElectromigrationPiezoelectricity
Chemical potentialDufour effectGalvanic cellFick's lawOsmosis
StressThermoelasticityPiezoelectricityOsmosisHooke's law

Example: Fluid system

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The fundamental equation

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The basicthermodynamic potential is internalenergy. In a simplefluid system, neglecting the effects ofviscosity, the fundamental thermodynamic equation is written:dU=TdSPdV+μdM{\displaystyle \mathrm {d} U=T\,\mathrm {d} S-P\,\mathrm {d} V+\mu \,\mathrm {d} M}whereU is the internal energy,T is temperature,S is entropy,P is the hydrostatic pressure,V is the volume,μ{\displaystyle \mu } is the chemical potential, andM mass. In terms of the internal energy density,u, entropy densitys, and mass densityρ{\displaystyle \rho }, the fundamental equation at fixed volume is written:du=Tds+μdρ{\displaystyle \mathrm {d} u=T\,\mathrm {d} s+\mu \,\mathrm {d} \rho }

For non-fluid or more complex systems there will be a different collection of variables describing the work term, but the principle is the same. The above equation may be solved for the entropy density:ds=1Tdu+μTdρ{\displaystyle \mathrm {d} s={\frac {1}{T}}\,\mathrm {d} u+{\frac {-\mu }{T}}\,\mathrm {d} \rho }

The above expression of the first law in terms of entropy change defines the entropicconjugate variables ofu{\displaystyle u} andρ{\displaystyle \rho }, which are1/T{\displaystyle 1/T} andμ/T{\displaystyle -\mu /T} and areintensive quantities analogous topotential energies; their gradients are called thermodynamic forces as they cause flows of the corresponding extensive variables as expressed in the following equations.

The continuity equations

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The conservation of mass is expressed locally by the fact that the flow of mass densityρ{\displaystyle \rho } satisfies thecontinuity equation:ρt+Jρ=0,{\displaystyle {\frac {\partial \rho }{\partial t}}+\nabla \cdot \mathbf {J} _{\rho }=0,}whereJρ{\displaystyle \mathbf {J} _{\rho }} is the mass flux vector. The formulation of energy conservation is generally not in the form of a continuity equation because it includes contributions both from the macroscopic mechanical energy of the fluid flow and of the microscopic internal energy. However, if we assume that the macroscopic velocity of the fluid is negligible, we obtain energy conservation in the following form:ut+Ju=0,{\displaystyle {\frac {\partial u}{\partial t}}+\nabla \cdot \mathbf {J} _{u}=0,}whereu{\displaystyle u} is the internal energy density andJu{\displaystyle \mathbf {J} _{u}} is the internal energy flux.

Since we are interested in a general imperfect fluid, entropy is locally not conserved and its local evolution can be given in the form of entropy densitys{\displaystyle s} asst+Js=sct{\displaystyle {\frac {\partial s}{\partial t}}+\nabla \cdot \mathbf {J} _{s}={\frac {\partial s_{c}}{\partial t}}}wheresc/t{\textstyle {\partial s_{c}}/{\partial t}} is the rate of increase in entropy density due to the irreversible processes of equilibration occurring in the fluid andJs{\displaystyle \mathbf {J} _{s}} is the entropy flux.

The phenomenological equations

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In the absence of matter flows,Fourier's law is usually written:Ju=kT;{\displaystyle \mathbf {J} _{u}=-k\,\nabla T;}wherek{\displaystyle k} is thethermal conductivity. However, this law is just a linear approximation, and holds only for the case whereTT{\displaystyle \nabla T\ll T}, with the thermal conductivity possibly being a function of the thermodynamic state variables, but not their gradients or time rate of change.[dubiousdiscuss] Assuming that this is the case, Fourier's law may just as well be written:Ju=kT21T;{\displaystyle \mathbf {J} _{u}=kT^{2}\nabla {\frac {1}{T}};}

In the absence of heat flows,Fick's law of diffusion is usually written:Jρ=Dρ,{\displaystyle \mathbf {J} _{\rho }=-D\,\nabla \rho ,}whereD is the coefficient of diffusion. Since this is also a linear approximation and since the chemical potential is monotonically increasing with density at a fixed temperature, Fick's law may just as well be written:Jρ=DμT{\displaystyle \mathbf {J} _{\rho }=D'\,\nabla {\frac {-\mu }{T}}}where, again,D{\displaystyle D'} is a function of thermodynamic state parameters, but not their gradients or time rate of change. For the general case in which there are both mass and energy fluxes, the phenomenological equations may be written as:Ju=Luu1T+LuρμT{\displaystyle \mathbf {J} _{u}=L_{uu}\,\nabla {\frac {1}{T}}+L_{u\rho }\,\nabla {\frac {-\mu }{T}}}Jρ=Lρu1T+LρρμT{\displaystyle \mathbf {J} _{\rho }=L_{\rho u}\,\nabla {\frac {1}{T}}+L_{\rho \rho }\,\nabla {\frac {-\mu }{T}}}or, more concisely,Jα=βLαβfβ{\displaystyle \mathbf {J} _{\alpha }=\sum _{\beta }L_{\alpha \beta }\,\nabla f_{\beta }}

where the entropic "thermodynamic forces" conjugate to the "displacements"u{\displaystyle u} andρ{\displaystyle \rho } arefu=1T{\textstyle \nabla f_{u}=\nabla {\frac {1}{T}}} andfρ=μT{\textstyle \nabla f_{\rho }=\nabla {\frac {-\mu }{T}}} andLαβ{\displaystyle L_{\alpha \beta }} is the Onsager matrix oftransport coefficients.

The rate of entropy production

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From the fundamental equation, it follows that:st=1Tut+μTρt{\displaystyle {\frac {\partial s}{\partial t}}={\frac {1}{T}}{\frac {\partial u}{\partial t}}+{\frac {-\mu }{T}}{\frac {\partial \rho }{\partial t}}}andJs=1TJu+μTJρ=αJαfα{\displaystyle \mathbf {J} _{s}={\frac {1}{T}}\mathbf {J} _{u}+{\frac {-\mu }{T}}\mathbf {J} _{\rho }=\sum _{\alpha }\mathbf {J} _{\alpha }f_{\alpha }}

Using the continuity equations, the rate ofentropy production may now be written:sct=Ju1T+JρμT=αJαfα{\displaystyle {\frac {\partial s_{c}}{\partial t}}=\mathbf {J} _{u}\cdot \nabla {\frac {1}{T}}+\mathbf {J} _{\rho }\cdot \nabla {\frac {-\mu }{T}}=\sum _{\alpha }\mathbf {J} _{\alpha }\cdot \nabla f_{\alpha }}and, incorporating the phenomenological equations:sct=αβLαβ(fα)(fβ){\displaystyle {\frac {\partial s_{c}}{\partial t}}=\sum _{\alpha }\sum _{\beta }L_{\alpha \beta }(\nabla f_{\alpha })\cdot (\nabla f_{\beta })}

It can be seen that, since the entropy production must be non-negative, the Onsager matrix of phenomenological coefficientsLαβ{\displaystyle L_{\alpha \beta }} is apositive semi-definite matrix.

The Onsager reciprocal relations

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Onsager's contribution was to demonstrate that not only isLαβ{\displaystyle L_{\alpha \beta }} positive semi-definite, it is also symmetric, except in cases where time-reversal symmetry is broken. In other words, the cross-coefficients Luρ{\displaystyle \ L_{u\rho }} and Lρu{\displaystyle \ L_{\rho u}} are equal. The fact that they are at least proportional is suggested by simpledimensional analysis (i.e., both coefficients are measured in the sameunits of temperature times mass density).

The rate of entropy production for the above simple example uses only two entropic forces, and a 2×2 Onsager phenomenological matrix. The expression for the linear approximation to the fluxes and the rate of entropy production can very often be expressed in an analogous way for many more general and complicated systems.

Abstract formulation

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Letx1,x2,,xn{\displaystyle x_{1},x_{2},\ldots ,x_{n}} denote fluctuations from equilibrium values in several thermodynamic quantities, and letS(x1,x2,,xn){\displaystyle S(x_{1},x_{2},\ldots ,x_{n})} be the entropy. Then,Boltzmann's entropy formula gives for the probabilitydistribution functionw=Aexp(S/k){\displaystyle w=A\exp(S/k)}, whereA is a constant, since the probability of a given set of fluctuationsx1,x2,,xn{\displaystyle {x_{1},x_{2},\ldots ,x_{n}}} is proportional to the number of microstates with that fluctuation. Assuming the fluctuations are small, the probabilitydistribution function can be expressed through the second differential of the entropy[6]w=A~e12βikxixk;βik=βki=1k2Sxixk,{\displaystyle w={\tilde {A}}e^{-{\frac {1}{2}}\beta _{ik}x_{i}x_{k}}\,;\quad \beta _{ik}=\beta _{ki}=-{\frac {1}{k}}{\frac {\partial ^{2}S}{\partial x_{i}\partial x_{k}}}\,,}where we are usingEinstein summation convention andβik{\displaystyle \beta _{ik}} is a positive definite symmetric matrix.

Using the quasi-stationary equilibrium approximation, that is, assuming that the system is only slightlynon-equilibrium, we have[6]x˙i=λikxk{\displaystyle {\dot {x}}_{i}=-\lambda _{ik}x_{k}}

Suppose we definethermodynamic conjugate quantities asXi=1kSxi{\textstyle X_{i}=-{\frac {1}{k}}{\frac {\partial S}{\partial x_{i}}}}, which can also be expressed as linear functions (for small fluctuations):Xi=βikxk{\displaystyle X_{i}=\beta _{ik}x_{k}}

Thus, we can writex˙i=γikXk{\displaystyle {\dot {x}}_{i}=-\gamma _{ik}X_{k}} whereγik=λilβlk1{\displaystyle \gamma _{ik}=\lambda _{il}\beta _{lk}^{-1}} are calledkinetic coefficients

Theprinciple of symmetry of kinetic coefficients or theOnsager's principle states thatγ{\displaystyle \gamma } is a symmetric matrix, that isγik=γki{\displaystyle \gamma _{ik}=\gamma _{ki}}[6]

Proof

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Define mean valuesξi(t){\displaystyle \xi _{i}(t)} andΞi(t){\displaystyle \Xi _{i}(t)} of fluctuating quantitiesxi{\displaystyle x_{i}} andXi{\displaystyle X_{i}} respectively such that they take given valuesx1,x2,,X1,X2,{\displaystyle x_{1},x_{2},\ldots ,X_{1},X_{2},\ldots } att=0{\displaystyle t=0}. Note thatξ˙i(t)=γikΞk(t).{\displaystyle {\dot {\xi }}_{i}(t)=-\gamma _{ik}\Xi _{k}(t).}

Symmetry of fluctuations under time reversal implies thatxi(t)xk(0)=xi(t)xk(0)=xi(0)xk(t).{\displaystyle \langle x_{i}(t)x_{k}(0)\rangle =\langle x_{i}(-t)x_{k}(0)\rangle =\langle x_{i}(0)x_{k}(t)\rangle .}

or, withξi(t){\displaystyle \xi _{i}(t)}, we haveξi(t)xk=xiξk(t).{\displaystyle \langle \xi _{i}(t)x_{k}\rangle =\langle x_{i}\xi _{k}(t)\rangle .}

Differentiating with respect tot{\displaystyle t} and substituting, we getγilΞl(t)xk=γklxiΞl(t).{\displaystyle \gamma _{il}\langle \Xi _{l}(t)x_{k}\rangle =\gamma _{kl}\langle x_{i}\Xi _{l}(t)\rangle .}

Puttingt=0{\displaystyle t=0} in the above equation,γilXlxk=γklXlxi.{\displaystyle \gamma _{il}\langle X_{l}x_{k}\rangle =\gamma _{kl}\langle X_{l}x_{i}\rangle .}

It can be easily shown from the definition thatXixk=δik{\displaystyle \langle X_{i}x_{k}\rangle =\delta _{ik}}, and hence, we have the required result.

See also

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References

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  1. ^abcOnsager, Lars (1931-02-15)."Reciprocal Relations in Irreversible Processes. I."Physical Review.37 (4). American Physical Society (APS):405–426.Bibcode:1931PhRv...37..405O.doi:10.1103/physrev.37.405.ISSN 0031-899X.
  2. ^Miller, Donald G. (1960)."Thermodynamics of Irreversible Processes. The Experimental Verification of the Onsager Reciprocal Relations".Chemical Reviews.60 (1). American Chemical Society (ACS):15–37.doi:10.1021/cr60203a003.ISSN 0009-2665.
  3. ^Yablonsky, G. S.;Gorban, A. N.; Constales, D.; Galvita, V. V.; Marin, G. B. (2011-01-01). "Reciprocal relations between kinetic curves".EPL (Europhysics Letters).93 (2) 20004. IOP Publishing.arXiv:1008.1056.Bibcode:2011EL.....9320004Y.doi:10.1209/0295-5075/93/20004.ISSN 0295-5075.S2CID 17060474.
  4. ^The Nobel Prize in Chemistry 1968. Presentation Speech.
  5. ^Wendt, Richard P. (1974). "Simplified transport theory for electrolyte solutions".Journal of Chemical Education.51 (10). American Chemical Society (ACS): 646.Bibcode:1974JChEd..51..646W.doi:10.1021/ed051p646.ISSN 0021-9584.
  6. ^abcLandau, L. D.; Lifshitz, E.M. (1975).Statistical Physics, Part 1. Oxford, UK:Butterworth-Heinemann.ISBN 978-81-8147-790-3.
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