Assume a single-phase ideal gas mixture in a closed parcel, with common temperature , total pressure , and molar species amounts . Define and volume mixing ratios , so . Ideal mixing makes partial pressure .
For a pure ideal species, , with molar volume . At fixed temperature, integration from standard pressure gives
The same logarithmic composition term follows from the ideal mixing entropy . Extensivity gives . Hence the Gibbs free energy of an ideal-gas mixture is
Equivalently, write each standard chemical term as , using molar enthalpy and entropy. For zero abundance the limit defines the extensive expression continuously.
The fractions alone do not specify the extensive Gibbs free energy: the total amount or an equivalent elemental inventory must also be fixed. Moreover, in a chemically closed reacting system need not remain constant; for example, hydrogenation of carbon monoxide changes the total molecular count while conserving atoms. Minimization is therefore over species amounts subject to elemental constraints, rather than over fractions with an artificially fixed molecular count. Nonideal gases require activities or fugacities; condensates contribute separate phase terms.
In the shock frame, integrate mass conservation, momentum conservation, and total-energy conservation across a thin interval containing the stationary normal shock wave. No mass, momentum, or energy is stored in the vanishingly thin interval, so each flux has the same value on both sides. For a perfect gas, the specific enthalpy is . The resulting Rankine-Hugoniot conditions for a perfect gas are
The momentum flux includes both transported momentum and pressure force. The energy flux includes kinetic energy and enthalpy, the latter accounting for internal energy and the work needed to push gas through the interval. Entropy production can occur inside the normal shock wave even though total energy is conserved.
Use the common-density, equal-volume-heat-capacity model implicit in the stated speed law. Let the liquid fraction be ahead of the melting front and behind it. Melting adds exactly the liquid needed to fill the newly created pores, so total mass conservation makes Darcy flux continuous. Consequently,
Here denotes Darcy velocity and the pore-liquid velocity in the stationary rock frame. Treating the pore-space increase as storage without its simultaneous melting source would incorrectly change the Darcy flux.
Relative to the cold unmelted material, the bulk enthalpy increase behind the front is : all phases gain sensible heat and the melted ice consumes latent heat. The advective heat-flux difference is . Applying the Rankine-Hugoniot condition to this energy balance therefore gives
so the advection-driven melting front in a porous matrix moves at
The advected latent contribution of the liquid is the same on both sides and cancels; the denominator measures sensible heating plus phase-change energy per unit bulk volume.
Put ahead of the front and behind. With viscosity , Darcy's law gives the planar pressure gradients and . Write the displacement as with , and take the unperturbed interface to be in its translating frame.
The liquid flux is divergence-free away from the interface, so the pressure perturbations are harmonic. The decaying normal modes are
Expanding pressure continuity at the displaced interface and matching normal Darcy flux gives
Hence
The common normal-flux perturbation is . The local enthalpy balance converts it into a front-speed perturbation, . Thus the melting-front instability due to permeability contrast has
For a signed transverse wavenumber, replace by .
For a simple compressible system with fixed particle number, the first law is
Define the enthalpy by . Then
Thus has natural variables and
Equality of mixed partial derivatives gives the Maxwell relation
Integrate each conservative ideal magnetohydrodynamics law through a thin pillbox around the stationary shock. Mass conservation gives
The MHD momentum-flux tensor is
Its normal and tangential components give
where is total pressure. The solenoidal condition gives , while steady Faraday's law gives continuity of tangential electric field,
Finally, material energy flux plus the normal Poynting vector component gives
where is specific enthalpy per unit mass.
Gravity is a bounded volume force, so its integral across a shock whose thickness tends to zero vanishes. Viscosity and resistivity inside the layer may produce entropy; consequently entropy flux need not be equal on both sides, although the second law requires nonnegative net entropy production.
The three jumps express conservation of mass flux, normal and tangential momentum flux, and total enthalpy (energy) flux across the stationary shock.
Polytropic enthalpy 2026-10-06
For with , the specific enthalpy relative to vacuum is . It obeys and . The vacuum reference is fixed when these equations are combined with the polytropic equation of state.
Specific enthalpy Created 2026-09-25 Updated 2026-10-06
Specific enthalpy is enthalpy per unit mass. For a simple compressible fluid of fixed composition, the first law of thermodynamics gives
where is temperature, is specific entropy, is pressure, and is mass density. Along an isentropic flow, . For a perfect gas with constant specific-heat ratio , .