For an ice layer between freshwater and cold brine, set and use solutal similarity positions , . A linear ice temperature, two Stefan conditions and interfacial salt conservation determine both negative interface constants. As with fixed latent-to-sensible heat ratio , but . Freezing above occurs over the thermal diffusion scale, while dilution-driven melting below has the much shorter solutal scale.
For and latent-to-sensible heat ratio with , put , , and . The steady heat equation becomes in the mush and in the liquid. Matching temperature and heat flux at , with and liquid temperature far above, gives
The latent heat modifies the mush's effective thermal decay rate and therefore its thickness.
Use undercooling , solidification attachment mobility , velocity scale , length and time . Let be the latent-to-sensible heat ratio, , and . In the one-sided liquid-diffusion model, a travelling planar front has and . For a corrugation , the decaying thermal perturbation is , with and the branch . The displaced kinetic condition gives . The displaced Stefan condition gives . Eliminating proves the displayed dispersion relation. Neglect of solid-side perturbation heat flux is part of this model.
Write , and . The requested model neglects density differences and uses the same thermal transport coefficients in the interfacial balances. Let and . With no imposed heat gradient in the fresh liquid, its temperature remains . The prescribed linear temperature in the ice is
The salt and temperature fields in the lower liquid satisfy diffusion equations, and . For constant interfacial values and the proposed similarity solution, their decaying solutions are
These follow by substituting a variable into the diffusion equation, which gives ; integrating gives the complementary error function. Their values at and at infinity give the required boundary data.
For the upward-moving fresh-water/ice boundary, the Stefan condition is : negative means fresh water freezes. At the lower boundary the signed heat balance is
Salt cannot enter the pure ice. With no bulk liquid motion its interfacial conservation law is
The derivatives and interface velocities are
Define . Substitution into all three balances gives
Together with , these determine the interfacial constants. In particular .
The physical branch has . Since is negative at negative arguments, the salt relation gives : lower-surface melting dilutes the brine. Combining the two heat balances eliminates the ice gradient and gives
Thus . The interface is at local liquidus equilibrium with diluted brine, while the undiluted far-field brine remains above its own liquidus. The similarity model describes a layer starting with zero thickness, or the long-time limit when an initial finite thickness no longer sets the dominant scale.
For the small-diffusivity-ratio limit, put and , keeping and the imposed concentrations fixed. Seek and . Then and . The upper heat balance gives
In the lower balance the two terms of order must cancel, giving
Consequently
and . Adding the two temperature differences yields . The negative root is
The resulting lies strictly between zero and . The salt relation therefore determines a finite negative , confirming its scaling. The top interface travels on the thermal scale , whereas the lower melting interface travels on the shorter solutal scale . This is the brine-ice sandwich with disparate diffusion scales; is the latent-to-sensible heat ratio, the reciprocal of the usual sensible-to-latent Stefan number convention.
Figure 1.
Similarity temperature and concentration profiles, local liquidus and ice-brine phase-diagram path
. Details.
The sketches show constant fresh-water temperature, a declining linear ice temperature, and a much broader thermal than solutal boundary layer in the brine. Concentration is zero in freshwater and pure ice, jumps to across the lower interface, and rises to . Accordingly the local liquidus is on the salt-free side, jumps to and falls rapidly to . In the phase diagram, the brine starts on the liquidus at and ends above it at ; the pure ice has concentration zero, and the interface tie-line joins it to the diluted brine.
Physically, the cold saline liquid permits freshwater to freeze above, but salt lowers the liquidus and allows the existing ice to melt into brine below even though that brine is colder than . Dilution raises the lower interfacial freezing temperature. Heat released by upper freezing supplies the lower melting and the conductive loss to the colder deep brine. With , upper freezing exceeds lower melting and the ice layer thickens as .
Let be the particle radius and the supercooling. Use spherical symmetry, constant thermal properties, equal phase densities , and negligible fluid advection. Let be latent heat per unit mass, the liquid specific heat, its thermal conductivity and its thermal diffusivity. The exterior temperature satisfies the radial heat equation
with for , and as .
The Gibbs-Thomson effect gives curvature-induced melting-temperature depression. For a spherical interface write
where is solid-liquid interfacial energy per area and the factor two is the sphere's curvature . Here in the thermodynamic formula is an absolute temperature. The notation also permits a given measured capillary coefficient without requiring its microscopic derivation.
In the one-phase Stefan problem, the solid has no internal heat flux and the Stefan condition is
The sign follows from heat balance: positive outward liquid heat flux releases latent heat as the solid grows. If the solid's thermal storage is retained, its temperature instead satisfies its own radial heat equation, , and . The two-phase condition is . It reduces to the one-phase condition in the quasistatic limit because a regular harmonic temperature inside a sphere is spatially constant. An initial solid temperature profile is additional data for a fully time-dependent two-phase problem.
Two reciprocal Stefan number conventions are common. The large parameter appropriate to the requested slow-interface limit is the latent-to-sensible heat ratio
It measures the energy required for phase change relative to cooling or heating by the supercooling. The often-used sensible-to-latent definition is . Thus “large Stefan number” here means large , not large in that other convention.
The thermal diffusion time for scale is , whereas the interface time is . More explicitly, with , and slow time , the liquid equation is
For , temperature therefore equilibrates before the radius changes appreciably. The quasistatic spherical Stefan problem with capillarity has a harmonic exterior temperature, fixed by its interface and far-field values:
The small initial diffusion adjustment is omitted at this order. Inserting into the Stefan condition gives
This is the critical radius for a supercooled spherical seed. For , the interface is warmer than the liquid and loses heat, driving growth. For , its curvature-depressed interface temperature is colder than the liquid, so heat enters and the solid melts. At , the uniform temperature supplies an equilibrium radius. It is unstable, since the radius-velocity derivative there is . For a growing particle with , increases asymptotically as .
For a subcritical particle the radius decreases monotonically and remains below . Hence
It cannot remain positive beyond , proving finite-time extinction of a subcritical spherical seed. The exact extinction time in the reduced model is obtained by separating variables:
With , this is
Near disappearance, the capillary term dominates and , so . For , the lifetime is ; it diverges logarithmically as , consistently with the unstable equilibrium. The threshold and lifetime above are conclusions of the specified large- quasistatic continuum model, rather than an assertion that its approximation is uniform through every finite- shrinking-interface transient.
Use the one-sided thermal conduction model encoded by the requested dispersion relation: neglect solid-side perturbation heat flux, take equal phase densities, and let the normal point from solid into liquid. Write the isotropic linear kinetic undercooling law using the solidification attachment mobility :
Here is solid-liquid surface energy, is the sum of principal curvatures, and is absolute temperature. Positive curvature convex into liquid lowers the equilibrium freezing temperature through the Gibbs--Thomson relation. The planar base state has .
Set and define
The paper's is the latent-to-sensible heat ratio, the reciprocal of the common Stefan number convention. Below, velocities, lengths and growth rates are dimensionless in these scales. In the travelling coordinate , the liquid heat equation gives , while the bounded solid steady field is constant. Matching a decaying liquid profile to the Stefan condition gives
The kinetic undercooling condition is . Thus
The speed is constant for , determined by and the attachment coefficient in the specified scales. Thermal diffusivity sets the exponential decay length , not the selected speed. Including solid-side perturbation conduction would change the stability equation below.
For linear stability analysis, corrugate the interface to and write the liquid perturbation as . The liquid heat equation requires
For this graph the linearized curvature is . Evaluate the temperature on the displaced interface: its perturbation is . The kinetic undercooling law therefore gives
Likewise the derivative evaluated at the displaced surface is , with . The Stefan condition at perturbation order reads
Elimination proves the one-sided kinetic solidification dispersion:
The destabilizing term comes from a protrusion encountering colder liquid; capillarity and kinetic relaxation oppose it.
At , and the base liquid has no thermal contrast generated by latent heat. The interface obeys : positive surface energy damps all nonzero modes, while is neutral at this order. Here the thermal perturbation amplitude vanishes, so the auxiliary decay exponent is immaterial to that pure kinetic relaxation. At , and the formal limit gives
For it has a negative real branch and no growing branch; at the interface branch is neutral. Strictly, is a singular endpoint of the travelling profile: no finite-width stationary exponential connects to the far-field value zero. These stability statements describe the limit of the travelling-front model.
For , assume at small wavenumber. Expand
Substituting into the dispersion relation cancels on both sides and gives
At the capillary stability threshold for a kinetic freezing front , continuing the same expansion gives : the nonzero long waves are damped even at threshold.
For large wavenumber, multiply the dispersion relation by and eliminate using the thermal equation. The exact algebraic form is
It prevents the uncontrolled replacement when itself is of order . In the usual small-capillarity range the leading results are
For the second result, set in the cubic; its quadratic-order balance gives . Thus positive capillarity stabilizes sufficiently short waves. If also and , the useful reduced approximation is
its finite terms should not be treated as a uniform expansion for arbitrary fixed .
For completeness, large dimensionless capillarity has different balances. At , and . For , , so . At , the real branch reaches : for its growth rate is , and for that endpoint is exact. For at this boundary, or for , the selected real- normal mode ceases to exist at sufficiently large wavenumber; the full diffusion problem includes a thermal continuous spectrum and cannot be assigned a real isolated interface growth rate by this ansatz there. Indeed, writing the bulk thermal perturbation as reduces its heat equation to , whose half-line diffusion modes have decay rates for . The thermal branch endpoint is . Loss of a damped isolated interface mode is not a morphological instability.
The approximate instability condition is already clear from the long-wave coefficient: , equivalently . In fact it is exact for growing modes of the present one-sided model. At , let , so . The right side of the dispersion relation becomes
For real , the residual is strictly increasing, since
Therefore a unique positive root exists precisely when . For , the unstable band is
There are no unstable oscillatory roots hidden by this real-root test. Indeed, if and , the thermal equation implies . For , the imaginary parts of the two equations would require , contradicting . Thus growing modes have real and real .
Figure 1.
Growth-rate curves for a one-sided kinetic freezing front
. Details.
The sketch shows zero capillarity approaching the positive plateau , weak capillarity giving a positive band followed by short-wave damping, and threshold/stronger capillarity giving damping at every nonzero wavenumber. The zero-wavenumber mode is a translation. As with fixed positive , both the unstable bandwidth and the positive growth rates shrink to zero; the small-wavenumber expansion is not uniform in that limit.
Use a one-sided top-hat plume model with Boussinesq approximation and neglect the solid/liquid density difference in the interfacial volume source. Define the positive ablation speed , volume flux per unit wall span , and kinematic momentum flux . Let ambient entrainment per height be , with entrainment coefficient , and take for the salinity contribution to density. Conservation of volume and vertical momentum, with negligible wall stress and negligible vertical momentum of entering fluid, gives
Only the ocean-facing edge entrains. Using two edges would change the entrainment coefficient in these formulas.
To derive the heat balance, choose liquid specific enthalpy and solid specific enthalpy . A horizontal slab receives ambient volume with enthalpy , and solid mass-equivalent volume with enthalpy . Thus
Subtract and divide by :
Similarly, the incoming salt flux is , so . Subtracting proves
Both anomalies are negative for fresh, cold melt entering the ocean. These balances account for the heat needed to melt the entering ice, rather than treating it as already-liquid water at .
Now use , the large latent-to-sensible heat ratio convention of the paper. Put . The stated small plume-deficit limits allow us to replace plume by their ambient values in the diffusive interfacial fluxes. The Stefan condition and interfacial salt balance are then
For the compositional Péclet number , solve the second equation and impose the liquidus:
Substitution in the heat balance gives the diffusive glacier-ablation interface law
Here is the liquidus slope, unrelated to the surface-energy parameter of the previous question. If , and , the physical root is
It is positive when , exactly the condition that the ocean is warmer than its own liquidus. Since and ambient properties are fixed, is constant with height in this approximation.
For the melting-driven saline wall plume, measure height from a virtual origin. The integrated anomaly balances are
In the specified small-deficit regime the meltwater volume is negligible compared with entrainment. Indeed, the solution below gives , so a small compositional plume deficit implies . Thus retain for the leading power laws, although remains essential in the salt and heat sources. Try , . The salt deficit is proportional to , and the momentum balance has powers , hence . The volume balance gives , and the momentum coefficient gives . Therefore
These are entrainment-dominated power laws, not an exact solution with the term retained in the volume equation. They fail close to the virtual origin, where the formal temperature and salinity deficits diverge. Their buoyancy source is distributed melting along the wall, unlike a line plume with a constant buoyancy flux from a localized source.
Figure 1.
Temperature and salinity from the ice interface through the wall layer and plume
. Details.
The profiles rise from across the laminar boundary layer to the almost-ambient plume values , then approach across the entraining edge. The sketch uses the linear-gradient approximation implicit in the prescribed diffusive fluxes; it is not an exact normal advection–diffusion profile at large .
For ,
The last formula retains both first-order terms and is appropriate near the no-ablation threshold. Salt diffusion keeps the interface saline, and freezing-point depression allows ice dissolution in saline water even when . Latent heat is still needed, but the thermodynamic permission to ablate comes from the depressed liquidus; small does not mean a negligible energy cost.
For , and . Rapid production of fresh melt dilutes the interface, so its temperature approaches the pure-ice melting point. In the usual thermally driven regime and ,
This is predominantly thermal melting. More generally the retained large- balance is . For example, gives , which can be large while the driving term is still saline freezing-point depression. Thus the melting/dissolution interpretation must also consider the ocean's temperature relative to , not the compositional Péclet number alone.
Use a planar saline Stefan problem with upward coordinate , the initial contact at , and phase boundaries and enclosing pure ice, where . Fresh liquid occupies and brine occupies . We assume negligible bulk flow, equal constant mass density , specific heat capacity and thermal diffusivity in all regions, and zero salt content and salt transport in the ice. Equal densities remove phase-change volume flow; suppressing convection isolates the molecular-transport mechanism. Different material properties would change the numerical coefficients. Set for the common thermal conductivity and . Denote the brine salt diffusion coefficient by .
Use a linear ice liquidus, , with and the salt mass fraction. Assume the initial brine is a stable liquid, , and all concentrations considered are below the eutectic composition. Thus . These assumptions exclude independent nucleation in a supercooled brine or an eutectic system event, neither of which is specified by the initial data alone. Start with a negligible seed of ice and use local phase equilibrium without interfacial kinetics or curvature. Temperature differences may be in Celsius, since only differences enter this calculation.
Write
The paper calls a Stefan number; it is the latent-to-sensible heat ratio, reciprocal to another common Stefan number convention. At the lower phase boundary, define and let
The liquidus relation is .
A similarity solution gives an explicit calculation of the two positions. Put
and use , . The temperatures and salinities are
These error function and complementary error function profiles satisfy the heat equation and the salt diffusion equation, their far-field conditions, and the interfacial temperature conditions. The fresh-water temperature is constant because the interface and the far field are both at .
Salt conservation at the moving lower phase boundary requires
For upward motion this is dilution by melting salt-free ice, rather than salt rejection by freezing brine. Substitution gives the dilution function for a melting saline Stefan front:
For , , so the interfacial brine is fresher than the remote liquid.
The Stefan condition at the upper boundary is , since the fresh liquid has no temperature gradient. At the lower boundary it is
These signs follow from the jump in enthalpy: the upper front freezes liquid while a positive melts solid. With , they reduce to
Together with , these equations determine , and hence both positions, without discarding the salt-diffusion correction.
For the stated large latent-to-sensible heat ratio, the layer is thin relative to the thermal diffusion length. Expanding the thermal equations for gives
Consequently a useful leading calculation is
where the positive is obtained from
The left side decreases with while the right side increases, and their values at zero and infinity guarantee a unique positive root for large . Thus this leading calculation includes the translation of the lower boundary as well as the increasing thickness.
If the scale separation also obeys , the familiar simpler result is
with
This last simplification needs the logarithmic refinement . The algebraic ordering alone should not be used to discard an arbitrarily large logarithmic correction; the preceding coupled equations remain the appropriate calculation when that refinement is unavailable. This distinction is captured by large latent heat in a freezing and melting ice layer.
Figure 1.
Fresh-water freezing and basal ice melting with the temperature and salinity profiles on their distinct diffusion scales
. Details.
The illustration uses , and . Solving the full equations gives , and . It shows the ice layer between freshwater and cold brine, with both fronts advancing upward and a strongly diluted lower liquid boundary.
Figure 2.
Temperature-salinity trajectory from cold bulk brine to the ice liquidus and through salt-free ice to fresh water
. Details.
The phase diagram shows the spatial path from remote brine to the lower interface: temperature first changes over at almost unchanged salinity, then salinity changes over its much smaller diffusion scale at nearly constant temperature. The liquid path ends on the liquidus at ; the solid has and its temperature rises from to . The eutectic position is schematic, with in the illustration, and is not used in the calculation. A point initially in the fresh layer freezes when reaches it, cools in the ice, and later melts when reaches it. The inset indicates this temporal path in the opposite direction through the solid branch and into the liquid.
The mechanism is simultaneous upper freezing and lower melting, with net growth of the ice thickness. Cold brine accepts most of the latent heat released by upper freezing. Salt reaching the lower contact lowers its equilibrium melting temperature, and melting freshens that liquid until its liquidus is close to . The heat delivered through the ice supplies the much smaller melting demand there. The remote brine remains liquid even though it is below the pure-water melting temperature, because it lies above its own saline liquidus. Thus “cold” does not by itself decide which phase is stable. These conclusions apply while the layers remain effectively deep and the stated no-convection, pure-ice and phase-equilibrium assumptions hold.
For a stationary, uniformly permeable skeleton, Darcy law gives . Constant-density conservation of mass gives , hence the pressure is harmonic:
With uniform gravitational acceleration, the same argument applies to pressure after subtracting its hydrostatic part. The spherical calculation below neglects body-force variation and uses the excess pressure relative to the far field.
Set and . When a shell freezes, its pore mass decreases at rate ; the difference must leave as liquid. Since Darcy velocity is volume discharge per total area, not pore-fluid speed, the interfacial and radial balances give
The positive sign means outward expulsion by the expansion on freezing. Integrating Darcy law with gives
There is no liquid Darcy velocity in the ice-filled region.
To state a closed Stefan problem, let be the effective thermal conductivities of the frozen and unfrozen composites and their volumetric heat capacities. If the matrix mass density is , the common specific heat gives and . These material coefficients are not numerically specified. With , the thermal equations are
The exterior equation retains advected sensible heat. A more detailed mechanical-energy model adds the Darcy dissipation source ; its smallness at leading order is checked below. At the origin require , and at infinity require , . At the phase boundary impose temperature continuity, phase equilibrium and the Stefan condition:
These equations, the radial liquid-mass balance and Darcy law, together with an initial radius and compatible initial temperature fields, specify the moving-boundary model. No curvature correction is imposed. A vanishing initial seed corresponds to the leading growth law below with .
Write and , the latent-to-sensible heat ratio. A conductive interfacial balance gives . On length scale , the ratio of thermal diffusion time to growth time is consequently bounded by
It is small for with fixed porosity and comparable constituent densities and thermal properties. Very small porosity requires the sharper condition ; the bare heat-capacity ratio alone should not be used uniformly as . The advective-to-conductive ratio is
Even if mechanical heating is retained, its size relative to latent-heat release is . For fixed water properties this is also small as , consistently with the linearized Clausius-Clapeyron relation. Thus unsteadiness, thermal advection and mechanical heating are higher-order effects. The local leading temperature fields satisfy Laplace's equation. The approximation describes radii of order ; the distant transient diffusion tail supplies the far-field matching and need not be globally steady.
Regularity at zero and the interface/far-field values give
The Stefan condition becomes . Introduce the dimensionless pressure-feedback factor
Combining this heat balance with pressure-dependent phase equilibrium yields the growth and interface values:
This is pressure-limited spherical freezing in a porous medium. The interface values are constant during this leading solution, although changes at a fixed exterior radius.
As permeability of a porous medium decreases, increases: the interface pressure rises toward the finite value , while the interface temperature falls toward . Hydraulic resistance suppresses freezing through pressure-induced freezing-point depression. In the limit , ; a zero-seed radius grows as and tends to zero at fixed time. A finite seed instead hardly changes. At exactly zero permeability an incompressible rigid model cannot expel the expansion volume, so sustained growth stops; deformation or compressibility would require a different model.
Let measure distance inward from the surface. While , curvature is negligible and this is a planar two-phase Stefan problem. Use a common reference mass density , specific heat capacity , thermal conductivity and thermal diffusivity ; retain the mass density differences only in the subsequent buoyancy estimates. Define , , and . The paper's parameter is the latent-to-sensible heat ratio, reciprocal to the more usual Stefan number.
For superheated two-phase Stefan similarity, solving with , and gives the Neumann solution of the Stefan problem. With ,
The solid expression holds for and the liquid expression for . The interface gradients inserted in the Stefan condition determine the positive constant :
The right-hand bracket decreases from infinity and crosses zero, while the equivalent left-hand side increases, proving uniqueness. The liquid-side flux subtracts from the roof cooling: it is heat brought to the interface by the superheated interior.
For large , . Keeping the superheat term while using and yields . Hence the small-interface-parameter growth with liquid superheat approximation is
The solid temperature is approximately linear across its thin crust, while the liquid thermal boundary layer has thickness of order . For fixed superheat and , ; for , . This retains the strong suppression of growth by a very hot interior.
To estimate overturn, take local gravitational acceleration at the roof. The liquid's mass density contrast is , while the solid contrast is . A liquid thermal layer of thickness has Rayleigh number . As , it reaches its critical value after a time scaling as
In viscous overturn of a dense crust, an unstably stratified viscous crust has a Rayleigh-Taylor instability growth time of order . Setting this equal to its age, with , gives
These are formation-to-overturn times. A specified critical liquid Rayleigh number multiplies by ; logarithmic amplification and geometrical constants also affect the crust estimate. They are omitted for the requested order-of-magnitude scaling.
The given numbers yield , and . Thus
Liquid thermal overturn is enormously faster than crustal overturn throughout the stated range. Even a critical-Rayleigh prefactor of order does not change that ordering. Since is not asymptotically large, low-superheat coefficients from the permitted approximation are only approximate. At the upper end , so the linear thermal-density approximation also ceases to be quantitatively credible; that endpoint is a formal scaling estimate under the supplied constant-property model. At a common age the instantaneous viscous instability-time ratio instead scales as ; it should not be confused with the above formation-time ratio.
For a boundary-layer renewal model, the liquid layer reaches . Its cycle-averaged thermal flux is consequently
If a critical Rayleigh number is retained, insert a factor . Averaging the diffusive flux over a cycle only changes an order-one coefficient. The crust reaches
so its average solid-volume flux per roof area is the crust-removal flux
The corresponding mass flux is and latent-heat flux is . This independent-cycle estimate is a scale for a crust that reaches overturn thickness and is then renewed. Because the liquid renews much more rapidly, in a hot interior its average heat flux can limit actual crust growth: the consistent interfacial budget is . A stalled crust would not realize repeated solid cycles. In a superheated interior, detached solid may also remelt; permanent core deposition is most directly justified in the late regime requested next.
At late times , liquid thermal buoyancy vanishes and . Thus
Assuming thin renewed crust, efficient sinking and constant asteroid radius, conservation of mass gives under the permitted equal-density approximation. Therefore the asteroidal core growth by crustal sinking law is
For a self-gravitating approximately uniform sphere, , so and a zero-seed core scales as . This law applies while the thin-crust renewal model remains valid and liquid remains available; it cannot continue beyond complete solidification. The specific numerical lifetime cannot be inferred without the absolute solid viscosity and conductivity.
Use the usual saline Stefan problem approximation: no bulk flow, salt-free ice with negligible salt transport, constant properties, equal phase densities, and the same thermal conductivity and thermal diffusivity in both phases. Write for specific heat capacity, for latent heat per unit mass, and . These thermal symmetries are needed for the arithmetic-mean interface temperature requested in the paper; unequal phase conductivities would give a weighted balance instead.
Set , , and . The heat equation and salt diffusion equation reduce to . Their similarity solutions, in terms of the complementary error function, are
These have the required interface values and far-field limits. At each fixed they recover the initial data as . The liquidus condition is .
Salt rejection and the Stefan condition give, with gradients evaluated on the appropriate sides of the interface,
For example, salt rejection is obtained by differentiating the total salt on a moving liquid interval: the moving lower endpoint removes , which must be supplied by diffusive transport away from the salt-free solid. Substitution, including the salt-rejection function for a saline Stefan front, gives the complete algebraic system for the diffusion-controlled iceberg growth and ablation:
The sign of distinguishes freezing from melting; neither sign should be excluded in the general similarity solution.
For , , and fixed and far-field temperatures, the thermal equation has leading right-hand side , while its left-hand side is . Hence
This is a leading-order balance, not an exact cancellation of latent heat. The resulting and the first algebraic equation determine the leading . A physical finite- branch requires ; if the mean temperature is positive, this salt-diffusion scaling cannot describe the leading solution. Likewise, a latent-to-sensible heat ratio diverging as changes the leading thermal balance.
Define and . Put and . Then , which will determine the freezing and constitutional supercooling conditions below.
Use , , and , the latent-to-sensible heat ratio. Transforming the heat equation to the fixed apparatus frame and substituting Darcy flux gives the exact steady mush equation
For , the solid fraction is . Since , the latent term remains leading order, whereas the correction is small. Define . The large-concentration thermal profile of a pulled mush then obeys
With and in the liquid,
The thermal conductivity agrees on both sides and the solid fraction vanishes at the mush–liquid interface, so there is no jump in latent production there: continuity of heat flux gives . Thus
The boundary value determines , as calculated next. The crystal fraction is obtained from the previous part's formula, with the temperature field understood to this leading asymptotic accuracy.
Figure 1.
Temperature and crystal fraction in a steadily pulled mush
. The leading large-concentration temperature field matches smoothly to the liquid at the top of the mush. The crystal fraction tends to zero there; the remaining liquid freezes at the eutectic front at the bottom. Details.
Melting raises permeability of a porous medium. An advancing protrusion therefore offers a less resistive path to hot liquid, attracting larger Darcy flux and receiving more heat. The resulting faster melting reinforces the protrusion: this is a reactive infiltration instability. A permeability decrease would reverse this feedback, while zero contrast gives no growth in this ideal model.
For positive contrast, the growth rate is proportional to transverse wavenumber, so the model has no finite fastest-growing wavelength. The latent-to-sensible heat ratio slows the front but supplies no short-wave cutoff. Finite thermal transport and a resolved melting zone can introduce a length scale; pore geometry eventually limits the continuum description. If interface curvature changes the equilibrium melting temperature through the Gibbs--Thomson relation, that can also oppose short-wave corrugations. The modified dispersion relation must include such effects before a preferred wavelength can be calculated; a length scale alone does not guarantee that every added mechanism selects one.
For a saline Stefan problem with common thermal properties, , and fixed latent-to-sensible heat ratio, set , and . A finite- similarity solution has . At the onset of constitutional supercooling, and the error in this mean is . The salt-rejection function for a saline Stefan front then gives , whereas . Comparing the actual temperature gradient to the liquidus gradient gives the displayed onset, with supercooling on the side of greater . For a freezing front at and , the ratio of these two gradients decreases into the liquid, so their interface comparison also decides whether a supercooled interval occurs anywhere ahead. The formula is an asymptotic criterion; finite- onset requires the full Stefan condition and salt balance.
The small- limit of superheated two-phase Stefan similarity gives , where and . For fixed superheat at large latent-to-sensible heat ratio, . For much larger superheat, . The approximation retains the leading effect of a hot interior and its coefficient need not be exact when is only order one.
For equal phase thermal properties, a roof undercooling and liquid superheat , the planar Stefan problem has interface . The solid error function profile and liquid complementary-error-function profile give . Here is the latent-to-sensible heat ratio. Liquid heat supplied to the interface reduces crust growth.