Abstract
The two-phase mixture model has been widely used to describe the performances of fluid flow and heat transfer within porous media with liquid phase change. However, this model was based on two important assumptions: the temperature is constant (T f = const) in two phase region, while fluid temperature is locally equal to the solid matrix temperature (T s = T f). These assumptions result in an inveracious numerical phenomenon, i.e.,: a thermal insulating layer within the porous matrix in numerical simulations. This numerical phenomenon is not real, because the solid matrix is made of thermal conductive material. To modify the mathematical model of the transpiration cooling problem with boiling, this paper presents an improved model, which is based on that the Gibbs free energy of liquid phase and vapor phase are equal in two-phase region. Temperature variation in two-phase region is considered, and fluid temperature is locally different from the solid matrix temperature (T s ≠ T f), therefore the local heat transfer through the convection between solid and fluid is considered as well. Numerical calculations of the transpiration cooling problem with boiling are carried out with the improved model. The numerical results such as the variations of temperatures of fluid and solid, the saturation and pressure of fluid within porous media, are reasonable, and the inveracious issue of the thermal insulating layer is successfully resolved.
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Abbreviations
- z :
-
Coordinate
- L :
-
Length
- T :
-
Temperature
- h :
-
Specific enthalpy
- k :
-
Thermal conductivity
- H :
-
Specific revised enthalpy
- c p :
-
Specific heat capacity
- s :
-
Saturation
- t :
-
Time
- \({\vec {u}}\) :
-
Velocity
- j :
-
Diffusive mass flux
- \({\langle \dot {n} \rangle}\) :
-
Volumetric mass rate of evaporation
- K :
-
Absolute permeability
- k r :
-
Relative permeability
- p :
-
Pressure
- \({\vec {g}}\) :
-
Gravitational constant
- d p :
-
Averaged particle diameter of porous media
- p c :
-
Capillary pressure
- q :
-
Volumetric heat generation rate induced by convection
- h sl :
-
Convective heat transfer coefficient between solid and liquid
- h sv :
-
Convective heat transfer coefficient between solid and vapor
- R :
-
Mole gas constant
- M :
-
Mole mass
- g :
-
Specific Gibbs free energy
- B :
-
Saturation equation associated with the phase state
- ṁ :
-
Mass flow rate of coolant
- Q :
-
Heat flux on the hot side surface
- D :
-
Discrete system of the equations
- N :
-
Nodes number
- Γ:
-
Effective diffusion coefficient
- ρ :
-
Density
- ɛ :
-
Porosity
- λ:
-
Relative mobility
- μ :
-
Kinetic viscosity
- σ :
-
Surface tension coefficient
- α :
-
Specific surface
- η :
-
Entropy
- ξ :
-
Intermediate variable
- ζ :
-
Intermediate variable
- χ :
-
Phase state
- s:
-
Solid
- l:
-
Liquid
- v:
-
Vapor
- f:
-
Fluid
- sat:
-
Saturated state
- eff:
-
Effective
- sf:
-
Solid–fluid
- 0:
-
Reference state
- in:
-
Inlet of porous media
- c:
-
Coolant tank
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Wei, K., Wang, J. & Mao, M. Model Discussion of Transpiration Cooling with Boiling. Transp Porous Med 94, 303–318 (2012). https://doi.org/10.1007/s11242-012-0006-0
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DOI: https://doi.org/10.1007/s11242-012-0006-0