In the heat-exchanger frame the crystal velocity is , while the liquid velocity is . The steady vertical mass flux is constant and equals in the fully solid eutectic material. Hence
This gives the density-change flow in a pulled mushy layer
The laboratory mixture volume flux is . In the pure liquid , while in the fully solid region and the material moves at . The liquid velocity formula applies wherever liquid exists; at solid fraction one there is no liquid phase to assign a velocity.
For a steady field in the apparatus frame, the time derivative in the translating crystal frame is . The given solute equation therefore becomes
Substituting the density-change flow in a pulled mushy layer reduces this to . Thus the solute conservation in a steadily pulled mush integrates to , using the zero solid fraction at the top boundary.
Set . The liquidus gives , so
In particular, at , and immediately above the eutectic temperature, where , the mush has . It becomes fully solid across the eutectic front 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.
Impose the eutectic temperature at in the large-concentration thermal profile of a pulled mush:
Therefore
The thickness is proportional to thermal diffusivity divided by pulling speed. Latent-heat release modifies the exponential decay rate through , while the far-liquid temperature fixes how far the profile can remain below the liquidus.

Articles by others on the same topic (0)

There are currently no matching articles.