Submitted:
01 November 2025
Posted:
03 November 2025
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Abstract
Keywords:
1. Introduction
2. Mathematical and Computational Model
2.1. Macroscopic Conservation Equations
2.2. Simplified 2D Geometrical Model of the Volumetric Forces
2.3. Identification of Zones of Different Grain Structures
2.4. Transport Properties and Closure Relationships
2.5. Computer Simulation and Solution Procedures
3. Credibility Analysis of the Analyzed Computer Simulation Models
3.1. Validation of the Model
3.2. Mesh Sensitivity Analysis
4. Simulation of the Pb-48wt.% Sn Centrifugal Casting – Results and Discussion
4.1. Comparison of the EP, EP-CP, and EP-FT Predictions of the Solute Macro-Segregation
4.2. The Role of Centrifugal Forces in the Developing Solute Macro-Segregation
5. Final Conclusions
Author Contributions
Data Availability Statement
Conflicts of Interest
Abbreviations
| Notation | Meaning |
| c | Specific heat, J·kg−1·K−1 |
| C | Concentration of chemical species, i.e., mass fraction, - |
| D | Solute mass diffusivity, m2·s−1 |
| f | Phase volumetric fraction, - |
| F | Force, N |
| g | Phase mass fraction, - |
| g | Gravity acceleration, m·s−2 |
| h | Heat transfer coefficient, W·m−2·K−1 |
| k | Thermal conductivity, W·m−1·K−1 |
| K | Permeability of the porous medium, m2 |
| kp | Equilibrium partition coefficient, - |
| L | Latent heat of fusion, J·kg−1 |
| ml | Liquidus slope, K·wt.%−1 |
| R | Distance of the gondola from the axis, m |
| T | Temperature, K |
| TE | Eutectic temperature, K |
| TM | Melting temperature of a solvent, K |
| V | Velocity vector, m·s−1 |
| Ṽ | Switching function value, - |
| α | Rotation angle of the gondola, rad |
| β | Rotation angle of a sample, rad |
| βC | Liquid solutal expansion coefficient, wt.%−1 |
| βT | Liquid thermal expansion coefficient, 1/K |
| λ2 | Secondary dendrite arm spacing, m |
| µ | Viscosity, kg·m−1·s−1 |
| ρ | Density, kg·m−3 |
| ω | Angular velocity, rad·s−1 |
| Subscripts | Meaning |
| cf | Centrifugal |
| coh | Coherency |
| C | Coriolis |
| g | Gravitational |
| L | Liquid fraction |
| m | Mixture |
| r | Resulting |
| ref | Reference value |
| S | Solid fraction |
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| Symbol | Units | Pb-48 wt.% Sn | Sn-10 wt.% Pb | |
|---|---|---|---|---|
| Initial mass fraction | C0 | wt%−1 | 48.0 | 10.0 |
| Density | Ρ | kg·m−3 | 9000.0 | 7000.0 |
| Specific heat | cL, cS | J·kg−1K−1 | 200.0 | 260.0 |
| Thermal conductivity | kL, kS | W·m−1K−1 | 50.0 | 55.0 |
| Viscosity | µ | kg·m−1·s−1 | 10-3 | 10-3 |
| Liquid thermal expansion coefficient | βT | K−1 | 10-4 | 6.0·10-5 |
| Liquid solutal expansion coefficient | βC | wt.%−1 | 4.5·10-3 | -5·10-3 |
| Latent heat | L | J·kg−1 | 53550 | 61000 |
| Diffusion coefficient (solid) | DS | m2·s−1 | 9·10-10 | 4.5·10-9 |
| Diffusion coefficient (liquid) | DL | m2·s−1 | 9·10-6 | 1·10-12 |
| Melting temperature of a solvent | TM | K | 600.65 | 505.15 |
| Liquidus slope | ml | K· wt.%−1 | -2.334 | -1.286 |
| Equilibrium partition coefficient | K | - | 0.307 | 0.0656 |
| Eutectic temperature | TE | K | 183.0 | 183.0 |
| Secondary dendrite arm spacing | λ2 | µm | 40.0 | 65.0 |
| Boundary conditions: | ||||
| Initial temperature | T0 | °C | 216.0 | - |
| Temperature of an ambient fluid | Tamb | °C | 25.0 | - |
| Heat transfer coefficient | h | W·m−2·K−1 | 400.0 | - |
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