Abstract
The mass transport and energy equations for a semi-infinite porous slab are solved using similarity variables and closed form functions to describe freezing with remelt at the interface. Heat and mass balance analyses give a transcendental equation for the unknown interfacial freezing velocity for solving on the computer. The solutions for the temperature and mass concentration are decoupled and solved analytically. The solution for convective boundary conditions is compared with that for Dirichlet boundary conditions. The progressive development of the solution with material thickness and change of functional time dependence and effect on the stability of nucleation is outlined. A discussion with biological adaptation to extreme cold and possible evolution of molecules in heat transfer regimes is included in light of the above.
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Abbreviations
- a :
-
Thermal diffusivity in Wolfram
- a 0 :
-
Distance of nearest vacant sites (of order 1 Angstrom)
- C Molar:
-
Concentration of moisture
- C i/C 3 :
-
Nondim concentration
- C 3 :
-
Critical point concentration
- Co Molar:
-
Concentration of bound substance
- C p :
-
Specific heat
- C s :
-
Concentration at x = 0
- C om :
-
Initial molar concentration of moisture (=C0)
- D 1, D 2, E 1, E 2 :
-
Constants of integration
- K i :
-
Effective thermal conductivity in region 1
- K ij K i/K j :
-
Thermal conductivity ratio
- l :
-
Latent heat
- L :
-
Nondim enthalpy (L/RT3)
- L diff :
-
Diffusive length
- Q 1 :
-
Nondimensional latent heat (Stefan constant)
- r :
-
Recondensation factor
- R :
-
Gas constant
- S(t):
-
Position of phase interface
- T 0 :
-
Initial temperature
- T i :
-
Temperature in region i
- T s :
-
Temperature at x = 0
- T m :
-
Temperature at freezing interface
- T ∞ :
-
Far field temperature
- U :
-
Transformation variable for decoupling
- v :
-
Velocity
- M :
-
Molecular weight
- T, T 3 :
-
Temperature, critical point temperature
- x :
-
Distance variable
- Z :
-
Nondimensional solution for concentration
- θ :
-
Nondim temperature
- Θ :
-
Temperature in spherical solution
- α i :
-
Effective thermal diffusivity in region i
- α mi :
-
Effective moisture diffusivity
- α 12 :
-
Thermal diffusivity ratio
- β, δ 1 :
-
Decoupling constants
- γ :
-
Surface tension
- ∆G :
-
Free energy
- ∆H :
-
Enthalpy
- ∆T :
-
Undercooling
- ε :
-
Porosity
- η :
-
Similarity variable x/(αt)1/2
- λ :
-
Nondim position of freezing interface
- ρ :
-
Density
- ω :
-
Volume fraction of adsorbed initial moisture
- MBP:
-
Moving boundary problem
- Ste:
-
Stefan Number = sensible heat/latent heat
- Bi:
-
Biot number = hL/k
- Nu:
-
Nusselt number, same functional definition as Biot number
- Sta:
-
Stanton number = h/(ρvc p) = ratio of heat transferred to thermal capacity
- \( {\text{erf}}\left( z \right) = \frac{2}{\sqrt \pi }\int\limits_{0}^{x} {e^{{ - \left( {x^{2} } \right)}} } {\text{d}}x \) :
-
erfc(z) = 1 − erf(z)
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Acknowledgements
This work started as a doctoral project suggested at NCSU under Prof. Michael Boles. The work on turbulent boundary layers was revived after similarities were observed in the equations and mechanisms. Inspirational discussions with Prof. Donald Coles of Caltech and Prof. Juan Oro of the University of Houston are also remembered and gratefully acknowledged. I am also grateful for meeting Prof. JBS Haldane, FRS, and his wife Dr. Helen Spurway Haldane, FRS, in Bangalore many years ago and having discussions about albino swordtail fish. The movie Forbidden Planet at that time, and the Star Trek series deeply influenced me, and I was an online SETI volunteer for some time. I am grateful to the referees for a critical reading of the manuscript and for pointing out various unclear areas.
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Basu, R. Stability of Interfacial Phase Growth in a Slab with Convective Boundary Conditions. JOM 68, 1679–1690 (2016). https://doi.org/10.1007/s11837-016-1909-y
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DOI: https://doi.org/10.1007/s11837-016-1909-y