1. Introduction
In recent years, the need to manufacture high-quality casting products has driven the improvement of traditional foundry technologies by applying the hyper-gravity field created by centrifugal forces. The idea has emerged from the demand of the aircraft engine industry, facing the problem of low castability of lightweight titanium alloys, causing the incomplete filling of thin-walled cavities of turbine blades under terrestrial gravity. Centrifugal and Coriolis forces in the rotating mold drive the liquid metal into thin cast parts (e.g., Humphreys et al. [
1]). Moreover, it has been soon revealed and confirmed by extensive experimental and theoretical research conducted in the last decades that hyper-gravity also significantly influences the melt flow and heat and solute transfer during solidification at both micro and macroscopic scales. Thus, it visibly affects a final cast’s grain structure and mechanical properties.
One of the major flaws of the alloy cast solidifying under terrestrial gravity is its chemical inhomogeneity, known as solute macro-segregation. This phenomenon is attributed to the solute segregation at the individual grains’ scale due to different solute solubility in the liquid and solid phases and then to convective transport of the excess solute, the solidification shrinkage, and the relative motion of the liquid and solid phases at the whole cast’s scale. Thus, the evolution of a non-uniform distribution of the solute concentration and highly solute-reach long and narrow channels, which post-solidification thermal manufacturing processes can hardly remove, considerably deteriorates the quality of alloy casting products.
In this context, manufacturing of metal alloy casts in the centrifugal field has attracted foundry engineers and researchers, as the high-speed rotation enhances melt flow and significantly alters the processes of heat and solute transfer at both the grain’s and the whole cast’s scales, thus changing the developing dendrite structures, solute distributions, and the macro-segregation pictures. Therefore, for the last decades, vast experimental and theoretical research has been conducted all over the world to comprehend better the role of strength and directions of centrifugal forces in complex transport processes occurring in metal alloy solidification and to search for appropriate conducting the centrifugal casting process to get the product of satisfactory grain structure and mechanical properties.
Bataille et al. [
2] experimentally examined the Pb-50wt.% Sn cast’s microstructure after the centrifugal directional solidification with the constant high gravity level (over 15 times higher than the terrestrial gravity). They reported that the enhanced buoyancy decreases the primary arm spacing (PAS), yielding grain microstructures similar to those attainable in microgravity.
Zimmermann et al. [
3] used the optically transparent organic alloy (Neopentylglycol-(D) Camphor) and the direct in-situ observation of dendritic structures developing during the alloy solidification at different gravity strengths with the range from 0 up to 10g. In the case of a low cooling rate and a laminar melt flow, almost the same growth velocities and primary arm spacing of the columnar dendrites were observed for all g-levels. However, with the growing cooling rate, the nucleation of many equiaxed grains is observed in the case of 10g centrifugal solidification, and the accompanied CET (Columnar-to Equiaxed Transition growth) develops earlier in both time and position than in the case of low g-values.
By the detailed metallographic examination and mechanical strength tests, Gan et al. [
4] analyzed the influence of very high super-gravity (from 1000g up to 5000g) on the spatial distribution of eutectic structures in the Al-14.5Si. They reported that with the increase of the gravity strength, associated with the long-range convective transfer of the solute, the eutectic Si is visibly refined, and the tensile strength, the yield strength, and the elongation of the alloy are much higher when compared to those when solidification is conducted in the terrestrial gravity.
You et al. [
5] used metallographic and electron-scanning microscopes to study the role of a very high hyper-gravity (up to 3000g), perpendicular to the terrestrial gravity direction, in the developing dendrite microstructures and the chemical inhomogeneity in the commercial Al7050 alloy. They observed diverse grain microstructures for the changing hyper-gravity levels. Thus induced, the enhanced liquid alloy convection augments the Zn, Mg, and Cu solutes concentration gradients along the direction of hyper-gravity, therefore enabling the development of columnar and equiaxed crystals of different sizes and the macro-segregation effects in various parts of the analyzed sample.
Yang et al. [
6] have experimentally compared grain microstructures of Al-Cu alloy samples after the finite stage of solidification in terrestrial gravity (g) and hyper-gravity (800g). In the highly enhanced gravity, they observed solute-reach regions at the bottom and negative segregation of Cu at the top of the samples. This chemical inhomogeneity is more severe with increasing Cu solute in the analyzed alloys.
Lv et al. [
7] investigated experimentally the role of horizontal centrifugation in modifying the microstructure of a wedge-shaped Al-Cu cast. A thorough analysis of measured temperatures and metallographic images of the cast microstructure and grain orientation leads them to conclude that increased centrifugal acceleration significantly decreases the average grain size and the secondary dendrite arm spacing.
Nelson et al. [
8] have used high-speed synchrotron tomography and elaborated sophisticated 3D mapping to observe the evolving composition and microstructures of Al-15wt.% Cu samples during solidification in the terrestrial gravity. They have focused on the role of gravity and the direction between the melt flow and the primary dendrite growth on the evolving microstructure, fragmentation, and macro-segregation. They have concluded that the refined microstructures are obtained when the melt flow direction caused by thermal and solute buoyancy forces is the same as the temperature gradient direction.
From those mentioned above and several other research papers available in the worldwide literature involving in-situ and real-time observations of various metal alloy samplings solidifying in the enhanced gravity field, it comes out that final grain structures and thermo-mechanical properties of the cast are subject to many mold and processing factors, such as cast dimensions, direction and speed of rotation and temperature gradient, the solidification rate, the composition of the molten alloy and others. So, for a high-quality product of hyper-gravity casting, it is essential to tailor this specialized manufacturing method by continuously monitoring and optimizing its process parameters. For this purpose, a complete understanding and detailed knowledge of multi-scale heat and mass transfer processes are needed, including the role of external forces in developing chemical inhomogeneity in the final product of centrifugal casting. However, such a complete study is not possible only through cumbersome, expensive, and time-consuming experiments (based mainly on examining in-situ products). Several advanced models of computer simulation of heat and mass transfer processes occurring at the scale of individual grains (the mesoscopic scale) and the whole casting product (the macro-scale) have been developed in the last two decades to assist this cognitive endeavor significantly.
Viardin et al. [
9] and Viardin et al. [
10] have carried out the 2D numerical simulations of the columnar dendritic growth and microstructure developing during the directional solidification of Ti-48 at% Al. They analyzed various levels (up to 20g) and two directions of hyper-gravity, namely parallel and antiparallel to the path of primary dendrites growth. In these mesoscopic calculations, they have applied the phase-field method ([
9,
10]) or the simplified model ([
10]), where an envelope with continuously varying solid fractions represents the complex shape of a single dendrite. The performed calculations have shown that the strength and orientation of hyper-gravity greatly influence the grain morphology and the primary dendrite arm spacing (PDAS), particularly in the case where the direction of a high-level gravity is opposite to the temperature gradient (to the growth direction). The upward melt flow around the dendrite tip, enhanced by centrifugal forces, causes unstable dendritic growth, leading to tip splitting, branching, and local changes in the dendrite growth direction.
Zhang et al. [
11], using the Cellular Automaton and the Lattice Boltzmann methods, analyzed the effect of hyper-gravity on the growth of single and multiple columnar and equiaxed dendritic crystals of the Al-4wt.% Cu alloy. The results of this numerical study confirm that the primary dendrite arm spacing (PDAS) and its growth rate, the crystal microstructure, and the solute segregation strongly depend on the hyper-gravity strength and direction. When the gravity direction is consistent with the path of the primary dendritic growth, the PDAS, the dendrite growth rate, and the channel segregation are augmented with the increase of the hyper-gravity level. When the hyper-gravity vector’s direction is opposite to the primary crystal growth direction, the PDAS is significantly reduced, and the refined microstructure of a cast is obtained.
The results of these mesoscopic computer simulations of metal alloy solidification and the relevant in-situ observations show that the melt flow modulated under the hyper-gravity conditions significantly affects the grain nucleation, interface instability, constitutional undercooling, dendrite arms spacing and growth of columnar and equiaxed crystals, their migration and the CET, and thus giving the potential for grain refinement.
But the chemical heterogeneity at the scale of individual grains, inherent to the difference of solubility at the liquid-solid interface and non-equilibrium solidification, while associated with the relative motion of the liquid and solid phases (caused by thermosolutal convection, solidification shrinkage, grains sedimentation) leads to the solute macro-segregation developing in a whole cast domain containing an enormous number of grains. Here, computer simulation models used at the grain’s scale would require a tremendous and unavailable burden of computer resources nowadays. Therefore, meso-macroscopic modeling has been developed, where key calculations are performed on the macroscopic scale, and information about the developing grains’ structures is transferred to the macroscopic model through the effective properties of the two-phase region, the so-called mushy zone. Several such multi-scale computer simulation models have been proposed in the last three decades to predict compositional macro-segregation of chemical species in terrestrial gravity conditions. Macroscopic conservation equations of mass, momentum, energy, and species concentration are based on the mixture theory (e.g., Bennon and Incropera [
12], Ni and Incropera [
13]) or volume averaging (e.g., Beckermann and Viskanta [
14]). The mushy zone is formed in non-isothermal alloy solidification, where the competing columnar and equiaxed/globular grain structures develop. Motionless columnar dendrites are immersed in a molten alloy; in the other part of the mushy zone, equiaxed/ globular grains are suspended or/and transported in the alloy melt, and the CET can develop in the proceeding solidification. Various models of the mushy zone’s permeability have been proposed and supplemented to the macroscopic calculations of the transport equations. Some researchers treat the whole two-phase region as Darcy’s porous medium using the Kozeny-Carman model of permeability (e.g., Založnik and Combeau [
15], Kumar et al. [
16], Cao et al. [
17]), the others distinguish zones of columnar and equiaxed grains, where different models of the resistance to melt flow are applied. In many research papers, these two different grain structures are identified by the inspection of the solid fraction value in the mushy zone (e.g., Chang and Stefanescu [
18], Ilegbusi and Mat [
19], Vreeman and Incropera [
20], Krane [
21]). When it exceeds the dendrite coherency point (DCP) value, Darcy’s flow model with the permeability concept is used; otherwise, the pseudo-viscosity [
18] or semi-solid medium [
19] models are applied. Alternatively, Banaszek and Seredyński [
22] have proposed the replacement of the DCP model used in the identification of different dendritic structures by the direct tracking of a virtual surface, being a locus of the columnar dendrite tips and moving according to the local law of crystal growth on a fixed non-structural control-volume mesh. They have compared both models in the prediction of the solute macro-segregation pictures of Pb-Sn alloys solidifying in the rectangular cavities under the terrestrial gravity and concluded that the predicted channel segregates are prone to the used control-volume mesh, the applied permeability formula, and the method of separating different dendritic structures within the mushy zone (Seredynski and Banaszek [
23]).
However, the research reported so far on computer simulations of transport processes accompanying the centrifugal casting is less extensive than that concerning the process in terrestrial gravity conditions. It is mainly concerned with the pouring process; only a few research papers have addressed the issue of the effect of the strength and direction of hyper-gravity on the solute inhomogeneity developing throughout the whole cast at different stages of the centrifugal investment casting.
Daloz et al. [
24] have developed a 2D axisymmetric multi-scale computer simulation model for the centrifugally cast Al-Ti cylindrical sample. The proposed simulation is based on the volume-averaged Euler-Euler two-phase approach, where macroscopic thermal and solute convection calculations are coupled with microscopic nucleation and crystal growth models. Based on the analysis of the strength of terrestrial gravity, Coriolis, and centrifugal forces, only the latter has been taken into account in the calculations. The coherency-point approach [
19] has been used to distinguish the zones of stationary columnar dendrites and moving equiaxed grains. The detailed analysis of the obtained outcomes has shown the significant influence of the alloy’s initial superheating, grain growth kinetics, and the motion of equiaxed grains on the developed macro-segregation pictures in the sample. Humphreys et al. [
1] have developed a comprehensive computer simulation of the mold filling and solidification of high-temperature titanium alloys under significant centrifugal forces. Their 3D computational model is based on the volume-of-fluid method for capturing a gas-liquid free surface and discretizing the transient high-velocity fluid flow, heat transfer, and solidification on finite volume unstructured meshes. Taking advantage of the developed model’s capability, the authors have focused on the formation and transport of bubbles and the air entrapments (creating shrinkage porosity) in the investment casting of the turbine blade and reported a good agreement of the numerically predicted macro-defects and their experimental pictures. Finite element software and experimental measurements (X-ray flaw detection, fluorescence analysis, and electron microscope scanning) have been used by Yang et al. [
25] to study the issue of the role of centrifugal forces on the filling process, microstructure and mechanical defects in investment casting of the Nb-TiAl alloy for turbine blades. Showing good consistency, the calculations and experimental results confirm that the centrifugal casting blade has fewer shrinkage porosities and cracks and a much finer microstructure. However, the paper has not addressed the role of thermosolutal buoyancy and the Coriolis acceleration in the development of macroscopic chemical inhomogeneity. Battaglioli et al. [
26] have developed a 2D computer simulation model for predicting the influence of gravity strength on the evolution of fluid flow, temperature, and grain structures during the directional solidification of Ti-Al alloy on a centrifuge. The model is based on a single set of transport equations in the solid-liquid mixture, discretized on a structural control-volume mesh in the plane perpendicular to the rotation axis. The front tracking procedure is applied to trace the developing columnar dendrites zone, where the porous medium model is exploited. The resulting numerical predictions for various angular velocities and different lengths of the centrifuge arm show the augmented thermal convection of the melt with an increasing level of centrifugal acceleration and the negligible impact of Coriolis forces on the melt flow when compared to the buoyancy encouraged by the centrifugal acceleration. This research study omitted the solute convection, and the macro-segregation is not analyzed. Tao et al. [
27] have developed the 3D macroscopic model for the centrifugal investment casting of large-size titanium alloy components. The proposed computer simulation is based on discretizing macroscopic mass, momentum, and energy transport equations on a non-conformal finite difference mesh. The authors have focused on analyzing the centrifugal filling process and developing shrinkage holes in the titanium alloy casing. Comparing the numerical simulation results with the X-ray pictures, they conclude that the centrifugal casting process does not show visible improvements in shrinkage defects compared to the gravity casting. The 3D numerical simulation of the directional columnar solidification of Ti-Al alloys (consistent with the configuration of ESA GRADECET experiments) is presented by Fernández et al. in [
28] and [
29]. The applied volume-averaging model accounts for thermo-solutal convection, centrifugal, and Coriolis accelerations when the temperature gradient along the cylindrical sample is antiparallel to the total apparent gravity (sum of centrifugal and terrestrial gravity). The Kozeny-Carman hydrodynamic permeability of the columnar mushy zone and Boussinesq’s model for thermo-solutal buoyancy forces have been adopted, along with the assumption of even densities and specific heats of the liquid and solid phases and the equilibrium model of microscopic solute diffusion (the lever rule model). The calculations show that Coriolis acceleration, although weak, breaks the symmetry of flow, visibly changing the aluminum segregation picture, and these changes are intensified with the centrifugation strength level. The research is, however, restricted only to the development of the columnar dendrites during directional solidification. Lv et al. [
7] have presented the numerical and experimental analysis of the mold-filling process and solidification of a wedge-shaped Al-Cu cast under horizontal centrifugation. Their micro-macroscopic model is based on the simulation, where the cellular automaton method is adopted to calculate the grain nucleation and coupled with the finite element calculations of macroscopic transport processes. The presented parametric analysis is concentrated only on the impact of centrifugal forces on the cast’s microstructure changes and confirms that the rotation speed’s increase and the higher cooling rate cause the reduction of grain average sizes and the secondary dendrite arm spacing, whereas the mold’s increased preheat temperature gives the opposite effect.
The combined experimental research and computer simulations have led to significant progress in understanding the role of enhanced melt flow in a centrifuge. Despite these two-decade efforts, more still has to be done to achieve a better quantitative understanding of complex multi-scale processes deciding about grains’ micro and macro structures of hyper-gravity casting products. Among still open scientific questions, there is the influence of the interaction between the enhanced flow of melt and the Coriolis acceleration on convection and the growth of solidification microstructures [
9,
10,
30], the mechanisms behind columnar crystals progress [
5], and the macro-segregation developing at different hyper-gravity casting stages [
6,
28,
30]. Also, since numerical modeling is a primary potential source of valuable information on enhancing the reliability of the whole casting process, improving the accuracy and trustworthiness of multi-scale computer simulations of solute segregation under the centrifugal and Coriolis forces remains a challenge. The enhanced mesoscopic simulations [
9,
10,
11], based on the Phase-Field Method or the Grain’s Envelope Model [
9,
10] or the coupled Cellular Automaton and Lattice Boltzmann methods [
11] give a deep insight and much better understanding of the impact of the strength and orientation of hyper-gravity and the augmented melt flow on the PDAS, the growth of single and multiple columnar and equiaxed dendritic crystals, and the other micro and mesoscopic characteristics of the mushy zone. On the other hand, the above-discussed combined meso-macroscopic simulations of centrifugal casting are mostly restricted to the analysis of the mold-filling process and mechanical defects (e.g., [
7,
25,
27]), and to the directional solidification with the imposed thermal gradient direction (e.g., [
26]); do not take into account the terrestrial gravity (e.g., [
24]), Coriolis acceleration (e.g., [
24,
25]), the thermo-solutal buoyancy (e.g., [
7,
25,
26,
27]) and the different dendritic structures and the CET developing in the mushy zone (e.g.,[
28,
29]).
So efforts should be continued to develop further advanced computer simulations involving more accurate predictions of the solute macro-segregation and channeling phenomena under hyper-gravity, where the melt flow process is more complex and changeable than in gravity casting, and thus to frame reliable correlations between super-gravity forces and the resulting grain structures and chemical and mechanical properties of the centrifugal casting product.
The presented paper is the authors’ contribution to this up-to-date research area, in which the alternative computer simulation of the meso-macroscopic solute segregation evolving in a metal alloy cast during centrifugal solidification is proposed. The simulation, based on the coupling of the single-domain enthalpy-porosity method with the front tracking approach (to distinguish different dendritic structures in the mushy zone), is used for the first time in the detailed study of the solute inhomogeneity in the hyper-gravity conditions. The simplified 2D model of the representative rotating plane is developed on the basis of the thorough analysis of all forces acting on a cast in the centrifuge and their projections on the plane. To calculate mass, momentum, energy, and solute transport within this domain, the EP-FT model proposed in [
23] has been extended by taking into account the centrifugal and Coriolis forces and performing calculations on general unstructured triangular control-volume collocated meshes. An in-depth parametric study has been carried out involving the impact of the cooling direction, gravity strength, and orientation on the development of the macro-segregation pictures, and the tendency to form freckles in solidifying Pb-Sn alloy castings. Moreover, the same calculations have been performed with the commonly used single-domain hybrid model, based on the coupling of the enthalpy-porosity model with the coherency point concept, and the predicted macro-segregation and channeling have been compared, and their similarities and differences widely discussed.
2. Mathematical and Computational Model
Macroscopic calculations of binary alloy centrifugal solidification are often built on the single continuum enthalpy–porosity model utilizing the classical two-phase mixture theory (e.g., [
12,
13]). During the cooling and solidification of an alloy’s cast, the two-phase zone (mushy zone) evolves, usually containing two distinguished regions of columnar and equiaxed grains. The former, having a strong directional nature, appears as a dense crystalline-like matrix filled with inter-dendritic liquid. In the equiaxed zone, grains freely grow, mutually influence, and move in the melt, and the CET phenomenon might occur. To account for different resistances to the melt flow occurring within these two diverse dendritic structures, Darcy’s porous medium model is commonly used in the columnar dendrite zone, whereas the slurry medium model is applied to the equiaxed grain zone. Therefore, it is necessary to distinguish regions of different grain structures in the computational model before applying distinct descriptions of the flow conditions. Two methods have been used to identify grain regions of varying flow conditions; they are coupled with the enthalpy-porosity model. The first one is the commonly used coherency point approach (e.g., [
19,
20,
21]), and the computational model is further referred to as the EP-CP (Enthalpy Porosity- Coherency Point). The second one, further called the EP-FT (Enthalpy Porosity – Front Tracking), involves the front tracking procedure to trace the envelope of columnar dendrite tips on finite volume meshes (e.g., [
22,
23,
26,
31,
32,
33]). The macro-segregation and channeling pictures developing in the centrifugal investment casting predicted by the EP-CP and EP-FT models are compared in this research.
2.1. Macroscopic Conservation Equations
A single set of the macroscopic conservation equations of mass, momentum, energy, and the solute transport in the liquid-solid mixture appears as
V, T, and C are the velocity vector, temperature, and solute concentration, respectively. Thermo-physical properties: ρ, k, c, μ, L, and D denote density, thermal conductivity, specific heat, dynamic viscosity, latent heat of fusion, and solute mass diffusivity, respectively. Indices S and L refer to the solid and liquid phases. g and f are phase volumetric and mass fractions, respectively; stands for the switching function, which equals 1 in the columnar dendrites zone and 0 elsewhere.
According to the mixture theory, the velocity, thermal conductivity, overall solute concentration, and solute mass diffusivity of the liquid-solid mixture are given by:
where C
L and C
S are the average solute concentrations, and D
L and D
S are the solute diffusivities in the liquid and solid phases, respectively.
The volumetric sources,
FV, in Eq. (2) are given by
The first and second terms in the square brackets refer to thermal and solute buoyancy forces described by the commonly used Boussinesq’s natural convection model. In a stationary coordinate system, they are multiplied by the terrestrial gravity acceleration vector, g, and constitute the gravity force, Fg. The second and third terms in the curly brackets express the centrifugal, Fcf, and Coriolis, FC, forces.
2.2. Simplified 2D Geometrical Model of the Volumetric Forces
The volumetric forces acting on a liquid volume in the rotating frame are three-dimensional; the terrestrial gravity works in the vertical direction, centrifugal acceleration acts radially concerning the centrifuge axis, and the Coriolis force operates in the horizontal planes.
The gondola with the furnace and the sample, mounted at the end of the rotating arm (
Figure 1), rotates with the angular velocity, ω, around the axis Z. The rotation angle of the gondola, α, depends on the ratio of the centrifugal force and the gravity force and can be derived with the formula
The resulting (acceleration) force, Fr, is the sum of the centrifugal, Fcf, and gravity forces, Fg, and is applied to the mass center of the gondola.
The rotation rate, ω, and the distance from the axis, R, are adjusted to ensure the required gravity acceleration level. Three values of gravity acceleration are considered: 1g, 5g, and 15g. For the first one, treated as the reference case, the rotation speed is obviously equal to 0.
In the presented study, centrifugal casting in a simplified layout is considered. The sample is positioned in the center of the gondola. The cuboid shape of the mold is assumed. The basic orientation of the sample is presented in
Figure 1, according to the Cartesian coordinate system x’, y’, z’ (
Figure 1a), fixed with the gondola, rotating around the axis Z. The length of the edge parallel to the z’ axis is much lower than other dimensions of the cavity, so the 2D geometry of the computational domain is assumed. Additionally, the interactions of the molten alloy with walls parallel to the x’-y’ plane are omitted, and the fluid velocity components in the z’ directions are set to zero.
In this paper, the relation between the direction of cooling and the resultant acceleration force is investigated, so various orientations of the sample are considered. To accomplish various heat dissipation directions, given with Q, the sample is rotated around the axis perpendicular to the x’-y’ plane and crossing the central point of the sample, marked as the rotation axis in
Figure 1b. For each case the rotation angle, β, is measured between the modified direction of the dissipated heat transfer, Q, and the resulting force,
Fr, as presented in
Figure 1c, and it is considered as a multiple of a 30-degree angle. The limiting values of angles 0° and 180° correspond to the cooling from the bottom and top, respectively. The size of the considered domain is 0.1 m in the x-axis direction and 0.06 m in the y-axis direction (
Figure 1c). The new coordinate system, namely x, y, z, describes the orientation of the system relative to the acceleration force.
The first and second terms in the curly brackets in Eq. (9) refer to the gravitational acceleration and the centrifugal forces, respectively, and their influence can be described with the resulting (acceleration) force, Fr.
The Coriolis force (the last term in Eq. (9)) may act outside of the plane x-y, so to account for the impact of that force in the considered 2D geometry, it is necessary to take the components of the Coriolis force cast in the x-y plane. However, for the highest enhanced gravity acceleration, 15g, and the assumed process parameters, ω = 30 rad/s, R = 2.42 m, and assumed maximum molten alloy velocity Vmax = 0.1 m/s, the Coriolis force magnitude is comparable to the gravity force, and 15 times lower than the resulting force. So, in the simplified analysis, neglecting the Coriolis force is justified.
2.3. Identification of Zones of Different Grain Structures
Two different approaches are used to identify zones of prevailing distinct grain structures within the mushy zone. The first one is the dendrite coherency point model (DCP), which is based on continuously examining a solid fraction value in the mushy zone during developing solidification. Darcy’s flow model with the permeability concept is used when the solid fraction exceeds a critical value, generally accepted as equal to the solid fraction at the temperature at which the growing dendrites begin to impinge upon each other and form the stationary coherent dendritic network. Otherwise, in the zone where small equiaxed dendrites float in the alloy melt, the slurry model is adopted. This approach has been commonly used in meso-macroscopic computer simulations of metal alloy solidification under terrestrial gravity (e.g., [
18,
19,
20,
21,
22,
23]) and by Daloz et al. [
26] in the numerical analysis of solute segregation in the centrifugally cast Al-Ti cylindrical sample. According to this methodology, the porous and slurry regions are identified with the switching function, Ṽ
coh, which depends on the solid fraction according to the formula (e.g., Chang and Stefanescu [
18])
where g
s,coh is the volumetric fraction of the solid phase when the grains start to impinge.
The main uncertainty arising when using the DCP model concerns the reliable estimation of the packing solid fraction value at the dendrite coherency point. The literature review shows that because of the lack of experimental data for various metal alloys, some authors misuse the DCP value determined experimentally by Arnberg et al. [
34] for only aluminum-based alloys, while others set its value arbitrarily. This parameter is also known as the coherency solid fraction (e.g., Ilegbusi and Mat [
19]), and is referred to as g
s,coh in this paper. The DCP solid fraction, g
s,coh, strongly depends on the alloy composition (e.g., [
34,
35]), and its assumed value has a significant impact on numerically predicted solute concentration fields and macro-segregation pictures (e.g., [
20,
21]). Moreover, Banaszek and Seredyński [
22] have shown that the use of the iso-line of constant solid packing fraction for distinguishing different grain structures is inaccurate, particularly at early stages of solidification when the formation of channel segregates develops much earlier than the CET appears, i.e., for smaller values of the solid fraction.
An alternative method for identifying zones of different dendritic structures is based on direct tracking of a virtual surface, being a locus of the columnar dendrite tips and moving on a fixed control-volume mesh during proceeding solidification according to the assumed crystal growth kinetics. This approach, originated by Browne and Hunt [
31] for the case of purely diffusive alloy solidification, has been further extended to modeling columnar and equiaxed binary alloy solidification driven by natural thermal convection [
32] and thermo-solutal convection [
33] on 2D structural control-volume meshes. Recently, Seredyński and Banaszek [
23] have generalized the front-tracking procedure to 2D unstructured control-volume meshes and used it to analyze the role of different permeability laws and various microstructure characteristic lengths on the numerically predicted solute macro-segregation developing during solidification of Pb-Sn alloys in the terrestrial gravity conditions. Battaglioli et al. [
26] have applied the front-tracking method in their 2D computer simulation of centrifugal directional solidification of Ti-Al alloy to study the role of enhanced gravity on the evolution of fluid flow, temperature, and grain structures. Their model is, however, restricted to a structural control-volume mesh and does not involve the solute transport, so the solute macro-segregation is not addressed.
In the presented study, for the first time to the authors’ best knowledge, the front-tracking approach, coupled with the macroscopic description of heat, momentum, and solute mass transport phenomena driving the binary alloy solidification, is used to address the issue of the role of hyper-gravity acceleration in the development of chemical inhomogeneity in a solidifying cast.
The main novelty of the EP-FT simulation model lies in tracking the envelope of columnar dendrite tips on a fixed control-volume unstructured mesh at the end of each subsequent calculation cycle of the transport processes conducted using the enthalpy-porosity (EP) model. This hypothetical interface of columnar dendrite tips is represented by a series of linear segments connected with massless markers, as shown in
Figure 2a. An i-th marker’s initial location,
, is known from the previous time step; the marker moves in the normal direction to the front towards the bulk liquid, according to the determined local undercooling, ΔT, and the assumed columnar dendrite growth law. The marker’s new position is determined as
and a new shape of the front is obtained by the interpolation between new locations of the markers (
Figure 2a). In the presented calculations, the columnar dendrite tip velocity, V
tip, is assumed to be independent of the acceleration level and is determined using the Kurz-Giovanola-Trivedi law [
36] and the least-square approximation to get
for the further analyzed Pb-48wt.% Sn alloy.
The front-position-based switching function, Ṽ
ft, is related to the position of the columnar front and is defined at a consecutive time step as the ratio between the dashed volume and the whole corresponding control volume (
Figure 2b). Control volumes crossed by the front have properties of both the slurry and porous media. The source terms in the momentum balance equation, Eq. (2), are activated in this region with the appropriate weights depending on the Ṽ
ft function. Based on the actual position of the columnar front, the Ṽ
ft is equal to zero in the bulk liquid and the slurry zone and to one in the fully porous medium. It smoothly changes between these limit values along the control volume crossed by the columnar front. The function Ṽ
ft is also used to calculate actual values of the phase velocities according to:
where for parameter Ṽ, the coherency switching function, Ṽ
coh, or the front-position-based switching function, Ṽ
ft, can be substituted.
More detailed information on procedures related to tracking of the front and its relation with emerging structures can be found in our previous papers, e.g., Seredynski and Banaszek [
23].
The initial position of the front is coincident with the cooled walls. In the case presented in
Figure 1, only one wall is cooled, located at x = 0, where x and y coordinates are related to the system rotated by angle β. The beginning of the front is positioned at the point (x, y) = {0.0, 0.06} and the end at the point (x, y) = {0.0, 0.0}.
2.4. Transport Properties and Closure Relationships
The system of macroscopic transport equations (Eqs. (1) – (4)) is based on the mixture theory approach, where a two-phase medium is treated as a pseudo-fluid with smoothly varying properties, and the local thermal, compositional, and mechanical equilibrium occurs on the scale of a single grain. Eqs. (5) – (8) gives the liquid-solid mixture’s properties as weighted averages of the phase-averaged properties. In the analyzed case, the lever-rule model of micro-segregation is used in calculations. The local thermodynamic equilibrium is assumed at the phase interface, so the following relation between solute concentrations holds: k
pC
L* = C
S*, where k
p is the equilibrium partition coefficient, C
L* and C
S* are the actual solute concentrations at the liquid and solid side of the interface, respectively. According to the assumed microsegregation model, both surface concentrations are equal to volume-averaged ones, namely C
S=C
S* and C
L=C
L*. The hydrodynamic interaction between the molten alloy and the columnar dendrite porous structure is described with the Kozeny-Carman relation
under the assumption that the micro-scale parameter, namely the secondary dendrite arm spacing, λ
2, is constant, and the porous structure is isotropic.
In Eq. (2), the solid phase viscosity is defined differently in the slurry and porous zones. In the former, it is determined based on the Ishii and Zuber [
37] rheological model, where the slurry dynamic viscosity equals:
, and is also a weighted average of solid and liquid viscosities
. In the porous zone, the solid phase velocity equals zero, so the third term on the right-hand side of Eq. (2) disappears. In the control volumes close to the interface between the porous and slurry regions, demarcated by the Front (EP-FT model), the switching function, Ṽ, is used to switch between viscosity models smoothly.
On the other hand, in the EP-CP model, the coherency solid fraction iso-line is captured, and the coherency switching function, ṼCP, is used to commute between viscosity models smoothly.
The local equilibrium process is assumed, where the hydrodynamic forces between phases are balanced, the locally averaged temperature is uniform at the scale of a single grain, and the steady-state solute transport across the phase boundary is assumed.
Material properties and boundary conditions used in the simulations are gathered in
Table 1.
2.5. Computer Simulation and Solution Procedures
The EP-CP and the EP-FT computer simulation models for the binary alloy centrifugal casting have been developed and implemented as in-house codes. The mixture mass, momentum, energy, and solute conservation equations, Eqs. (1)-(4), supplemented with the closure relations, Eqs. (5)-(11) have been discretized on a non-orthogonal triangular control-volume mesh, and the implicit Euler scheme has been used for marching in time. Since the computational mesh is non-orthogonal, the skew diffusion terms are taken into account, where gradients of the field quantities at the control volume’s faces are determined with the cell-based approximation scheme [
38]. The collocated mesh concept, where all parameters are stored in a control-volume centroid, has been adopted along with the Rhie and Chow scheme [
39] for local velocities at the cell faces, applied to avoid numerically generated spurious wavy modes of the pressure field. The first order upwind scheme [
40] has been used for the field variables on the control volume’s faces, and the fractional step computational algorithm [
41] has been applied to couple the pressure and velocity fields. In the EP-CP calculations, different grain structures and the associated distinct models of the melt flow resistance within the mushy zone are identified by the DCP model (see subchapter 2.4). On the other hand, in the EP-FT simulation model at each consecutive time step, after the iterative solving of the conservation equations (Eqs. (1)-(4)), the front tracking procedure is used. Zones of the columnar and equiaxed grains are recognized based on the most actual temperature and concentration fields. Next, the switching function is calculated for each control volume, and the solution procedure is continued at the next step for the updated structure of the mushy zone.
5. Final Conclusions
The paper discusses the search for accurate and computationally efficient meso-macroscopic numerical simulations of complex solute macro-segregation (with local channels of high solute content) developing in a solidifying binary alloy under super-gravity conditions in a centrifuge.
In this context, detailed comparisons have been performed between three different mesoscopic models of the flow resistance in the zone of coexisting various grain structures (the mushy zone).
In the commonly-used EP model, the whole mushy zone is treated as a Darcy’s porous medium; in two others, the regions of prevailing columnar or equiaxed grains are distinguished, allowing the identification of dynamically varying extents of these regions and a more precise simulation of melt flow conditions within the whole two-phase zone. In the EP-CP simulation, the coherency point concept is exploited; the EP-FT model is based on directly tracking a hypothetical interface separating the stationary columnar dendrites region from the super-cooled alloy melt with fluctuating equiaxed crystals. These mesoscopic models are coupled with macroscopic calculations of the transport processes based on the single domain enthalpy-porosity approach.
For this comparative analysis, the simplified 2D model of external forces acting on the gondola in the centrifuge is proposed, and the calculations have been performed for the rotating 2D rectangular sample filled with Pb-48wt.% Sn alloy for various hyper-gravity levels and different angles between the cooling direction and the enhanced gravity direction.
Thorough analysis of the Sn concentration and the solid fraction temporal fields predicted by the EP, EP-CP, and EP-FT simulations leads to the conclusion that the pictures of macro-segregation and local channeling strongly depend on the mesoscopic model used. The differences in the models’ results increase with the rise of the hyper-gravity strength. The columnar porous zone size predicted by the EP simulation is overestimated, particularly at early times of the mold cooling, as a consequence of treating the whole mushy zone as Darcy’s porous medium. The EP-CP calculations are highly sensitive to the assumed coherence value of the solid fraction and provide completely different pictures of the solute inhomogeneity with some complex structures of merged solid grains (see
Figure 10 and
Figure 11), which are not present in the calculations with lower coherency point value or the EP-FT model. Moreover, since the volumetric solid fraction varies in time, along the columnar dendrite front, and with the hyper-gravity strength and direction, it is disputable to use its constant value at the coherence point for distinguishing regions of different dendritic structures.
Therefore, the EP-FT model is the most reasonable choice for a reliable simulation of complex macro-segregation pictures, particularly in centrifugal alloy casting, where the melt flow, solute mass, and heat transport processes are significantly enhanced, influencing the evolving grain structure.
The model was positively validated by comparing its results with the AFRODITE experimental benchmark of the Sn-10wt%Pb alloy solidification in the terrestrial gravity, and its accuracy was verified by the mesh sensitivity analysis in the case of Pb-48wt% Sn alloy solidification in the centrifuge with 5g effective gravity acceleration. Then, the EP-FT model was used to address the issue of the role of centrifugal forces in the developing solute chemical inhomogeneity under enhanced gravity. The results presented in the paper confirm the significant impact of both the strength of hyper-gravity and the angle between the cooling direction and the enhanced gravity direction on the solute concentration distribution and the position and shape of the front separating different dendritic structures, the number and size of locally forming highly solute-rich channels.
The carried out analysis confirms the formation of complex interfaces between porous and slurry zones.
The deeper analysis of the centrifugal casting cases and accounting for Coriolis forces requires complete 3D modeling and better mesh refinement close to the front. Considering the above, future activities will be oriented to parallelize the code on GPU cards and develop 3D models on unstructured adaptive meshes to enable solidification simulation in more complex domains. Also, the impact of the relative density of the solid grains and molten alloy as well as the role of nominal alloy composition and related direction of thermal and solute buoyancy forces should also be addressed. There is also a need for more sophisticated benchmark experiments, allowing for a more thorough analysis of complex transport phenomena and the role of the direction of cooling.
Figure 1.
The schematic of the centrifuge arrangement: (a) the rotating gondola with the furnace and sample, and the orientation of the sample and the direction of heat dissipation at the reference sample position (right side); (b) the sample orientation in the gondola after rotation in the x’-y’ plane.
Figure 1.
The schematic of the centrifuge arrangement: (a) the rotating gondola with the furnace and sample, and the orientation of the sample and the direction of heat dissipation at the reference sample position (right side); (b) the sample orientation in the gondola after rotation in the x’-y’ plane.
Figure 2.
The schematic of (
a) the front tracking procedure on a fixed unstructured control-volume mesh [
23]; (
b) determination of the switching function.
Figure 2.
The schematic of (
a) the front tracking procedure on a fixed unstructured control-volume mesh [
23]; (
b) determination of the switching function.
Figure 3.
Schematic of the geometry and boundary conditions of the AFRODITE benchmark casting.
Figure 3.
Schematic of the geometry and boundary conditions of the AFRODITE benchmark casting.
Figure 4.
Comparison of solute concentration maps predicted with EP, EP-FT, and EP-CP models, for the selected times of the mold cooling.
Figure 4.
Comparison of solute concentration maps predicted with EP, EP-FT, and EP-CP models, for the selected times of the mold cooling.
Figure 5.
Comparison of solid fraction and temperature predicted with EP, EP-FT, and EP-CP models after 2000s of the cooling process.
Figure 5.
Comparison of solid fraction and temperature predicted with EP, EP-FT, and EP-CP models after 2000s of the cooling process.
Figure 6.
Cross-sections across the domain for the completely solidified cavity, determined at various elevations: (
a) 1 cm; (
b) 2 cm; (
c) 3 cm; (
d) 4 cm; € 5 cm; predicted with the EP, EP-CP and EP-FT models and compared to experimental (Hachani et al. [
44]) and numerical results (Zheng et al. [
46]) results.
Figure 6.
Cross-sections across the domain for the completely solidified cavity, determined at various elevations: (
a) 1 cm; (
b) 2 cm; (
c) 3 cm; (
d) 4 cm; € 5 cm; predicted with the EP, EP-CP and EP-FT models and compared to experimental (Hachani et al. [
44]) and numerical results (Zheng et al. [
46]) results.
Figure 7.
Comparison of solute concentrations in the completely solidified alloy: (
a) the X-radiography map of Pb concentration; (
b) its digitally processed picture [
44]; (
c) the EP; (d) the EP-FT; I the EP-CP (g
s,coh = 0.3) calculations, respectively. (a) and (b) are reprinted from publication [
44], with permission from Elsevier.
Figure 7.
Comparison of solute concentrations in the completely solidified alloy: (
a) the X-radiography map of Pb concentration; (
b) its digitally processed picture [
44]; (
c) the EP; (d) the EP-FT; I the EP-CP (g
s,coh = 0.3) calculations, respectively. (a) and (b) are reprinted from publication [
44], with permission from Elsevier.
Figure 8.
Impact of the mesh density on the Sn concentration (left column) and the solid fraction (right column) after 250 s of cooling.
Figure 8.
Impact of the mesh density on the Sn concentration (left column) and the solid fraction (right column) after 250 s of cooling.
Figure 9.
Sn concentration predicted with the EP, EP-CP, and EP-FT models at the selected times of the cooling process for the effective gravity of 1g and β-angle of 90°.
Figure 9.
Sn concentration predicted with the EP, EP-CP, and EP-FT models at the selected times of the cooling process for the effective gravity of 1g and β-angle of 90°.
Figure 10.
Sn concentration predicted by the EP-CP and the EP-FT, at the selected early times of the cooling process, for the effective gravity of 15g and β-angle of 90°.
Figure 10.
Sn concentration predicted by the EP-CP and the EP-FT, at the selected early times of the cooling process, for the effective gravity of 15g and β-angle of 90°.
Figure 11.
Volumetric solid fraction calculated by the EP-CP and the EP-FT, at the selected early times of the cooling process, for the effective gravity of 15g and β-angle of 90°.
Figure 11.
Volumetric solid fraction calculated by the EP-CP and the EP-FT, at the selected early times of the cooling process, for the effective gravity of 15g and β-angle of 90°.
Figure 12.
Comparison of Sn concentration predicted by the EP-FT and EP-CP (gS,coh= 0.15) models, for the selected times of mold cooling, in terrestrial gravity and β-angle of 180°—the heat is extracted from the mold’s top wall.
Figure 12.
Comparison of Sn concentration predicted by the EP-FT and EP-CP (gS,coh= 0.15) models, for the selected times of mold cooling, in terrestrial gravity and β-angle of 180°—the heat is extracted from the mold’s top wall.
Figure 13.
Comparison of the volumetric solid fraction predicted by the EP-FT and EP-CP (gS,coh= 0.15) models, for the selected times of mold cooling, in terrestrial gravity and β-angle of 180° - the heat is extracted from the mold’s top wall.
Figure 13.
Comparison of the volumetric solid fraction predicted by the EP-FT and EP-CP (gS,coh= 0.15) models, for the selected times of mold cooling, in terrestrial gravity and β-angle of 180° - the heat is extracted from the mold’s top wall.
Figure 14.
Volumetric solid fraction along the columnar dendrite tips front after 250s of cooling, for various gravity acceleration levels (1g, 5g, 15g), and β-angles: (a) 90° and (b)180°.
Figure 14.
Volumetric solid fraction along the columnar dendrite tips front after 250s of cooling, for various gravity acceleration levels (1g, 5g, 15g), and β-angles: (a) 90° and (b)180°.
Figure 15.
EP-FT predictions of the solute (Sn) concentration after 250s of cooling for various effective gravity accelerations, g*, and rotation angles, β. The direction of heat transfer through the cooled wall is marked with the blue arrow.
Figure 15.
EP-FT predictions of the solute (Sn) concentration after 250s of cooling for various effective gravity accelerations, g*, and rotation angles, β. The direction of heat transfer through the cooled wall is marked with the blue arrow.
Table 1.
Material properties and boundary conditions used in calculations.
Table 1.
Material properties and boundary conditions used in calculations.
| |
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 |
- |