PHASE-FIELD MODELING OF CONTACT MELTING IN BINARY ALLOYS Kartuzov V.V. 1, Bystrenko O.V. 1, 2 1

Similar documents
Phase. Gibbs Phase rule

Chapter 8. Phase Diagrams

Lecture 4: Thermodynamics of Diffusion: Spinodals

POURING THE MOLTEN METAL

The first law: transformation of energy into heat and work. Chemical reactions can be used to provide heat and for doing work.

CHEMICAL ENGINEERING AND CHEMICAL PROCESS TECHNOLOGY - Vol. I - Interphase Mass Transfer - A. Burghardt

Phase Equilibria & Phase Diagrams

Introduction to Materials Science, Chapter 9, Phase Diagrams. Phase Diagrams. University of Tennessee, Dept. of Materials Science and Engineering 1

9.11 Upon heating a lead-tin alloy of composition 30 wt% Sn-70 wt% Pb from 150 C and utilizing Figure

Thermodynamic database of the phase diagrams in copper base alloy systems

Lecture: 33. Solidification of Weld Metal

We will study the temperature-pressure diagram of nitrogen, in particular the triple point.

Lecture 3: Models of Solutions

k 2f, k 2r C 2 H 5 + H C 2 H 6

Lecture 19: Eutectoid Transformation in Steels: a typical case of Cellular

FUNDAMENTALS OF ENGINEERING THERMODYNAMICS

Lecture 22: Spinodal Decomposition: Part 1: general description and

CHEMISTRY STANDARDS BASED RUBRIC ATOMIC STRUCTURE AND BONDING

Chapter 12 - Liquids and Solids

Phase Transformations in Metals and Alloys

Integration of a fin experiment into the undergraduate heat transfer laboratory

Steady Heat Conduction

vap H = RT 1T 2 = kj mol kpa = 341 K

THREE MAIN SOLIDIFICATION REACTIONS OF VANADIUM MODIFIED T1 TUNGSTEN HIGH SPEED TOOL STEEL. Hossam Halfa

a) Use the following equation from the lecture notes: = ( J K 1 mol 1) ( ) 10 L

Statistical Mechanics, Kinetic Theory Ideal Gas. 8.01t Nov 22, 2004

LOGO. Modeling and Simulation of Microstructural Changes in Composite Sn-Ag-Cu Solder Alloys with Cu Nanoparticles

Understanding Plastics Engineering Calculations

Exergy: the quality of energy N. Woudstra

Dimensional analysis is a method for reducing the number and complexity of experimental variables that affect a given physical phenomena.

New Methods of Testing PCB Traces Capacity and Fusing

7. DYNAMIC LIGHT SCATTERING 7.1 First order temporal autocorrelation function.

1 The basic equations of fluid dynamics

A Strategy for Teaching Finite Element Analysis to Undergraduate Students

Gibbs Free Energy and Chemical Potential. NC State University

Thermodynamics. Chapter 13 Phase Diagrams. NC State University

Simulation of Transient Temperature Field in the Selective Laser Sintering Process of W/Ni Powder Mixture

OPTIMIZATION OF DIAMETER RATIO FOR ALPHA-TYPE STIRLING ENGINES

Introduction To Materials Science FOR ENGINEERS, Ch. 5. Diffusion. MSE 201 Callister Chapter 5

Express Introductory Training in ANSYS Fluent Lecture 1 Introduction to the CFD Methodology

LN Introduction to Solid State Chemistry. Lecture Notes No. 10 PHASE EQUILIBRIA AND PHASE DIAGRAMS

Final Exam CHM 3410, Dr. Mebel, Fall 2005

Phase Equilibrium: Fugacity and Equilibrium Calculations. Fugacity

DIFFUSION IN SOLIDS. Materials often heat treated to improve properties. Atomic diffusion occurs during heat treatment

Ravi Kumar Singh*, K. B. Sahu**, Thakur Debasis Mishra***

Design of heat exchangers

NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES

Thermodynamics of Mixing

Chapter 7 : Simple Mixtures

Electrochemical Kinetics ( Ref. :Bard and Faulkner, Oldham and Myland, Liebhafsky and Cairns) R f = k f * C A (2) R b = k b * C B (3)

Problem Set 3 Solutions

μ α =μ β = μ γ = =μ ω μ α =μ β =μ γ = =μ ω Thus for c components, the number of additional constraints is c(p 1) ( ) ( )

Phase Diagrams & Thermodynamics

E-nergies of Multiphaseion in N regions

The Fundamentals of Thermoelectrics

Chapter 18 Temperature, Heat, and the First Law of Thermodynamics. Problems: 8, 11, 13, 17, 21, 27, 29, 37, 39, 41, 47, 51, 57

Incorporating Internal Gradient and Restricted Diffusion Effects in Nuclear Magnetic Resonance Log Interpretation

A Solutal Interaction Mechanism for the Columnarto-Equiaxed Transition in Alloy Solidification

Turbulent mixing in clouds latent heat and cloud microphysics effects

Chapter 2. Derivation of the Equations of Open Channel Flow. 2.1 General Considerations

Chemistry 13: States of Matter

TWO-DIMENSIONAL FINITE ELEMENT ANALYSIS OF FORCED CONVECTION FLOW AND HEAT TRANSFER IN A LAMINAR CHANNEL FLOW

PERMEABILITY MEASUREMENT

EXIT TIME PROBLEMS AND ESCAPE FROM A POTENTIAL WELL

Heat Transfer and Energy

Chem 338 Homework Set #5 solutions October 10, 2001 From Atkins: 5.2, 5.9, 5.12, 5.13, 5.15, 5.17, 5.21

Stability of Evaporating Polymer Films. For: Dr. Roger Bonnecaze Surface Phenomena (ChE 385M)

6. 2. Unit 6: Physical chemistry of spectroscopy, surfaces and chemical and phase equilibria

REACTIONS IN THE SN CORNER OF THE CU-SN-ZN ALLOY SYSTEM

CHAPTER 9 Part 1. = 5 wt% Sn-95 wt% Pb C β. = 98 wt% Sn-2 wt% Pb. = 77 wt% Ag-23 wt% Cu. = 51 wt% Zn-49 wt% Cu C γ. = 58 wt% Zn-42 wt% Cu

HEAVY OIL FLOW MEASUREMENT CHALLENGES

Chapter 10 Phase equilibrium

Adaptive Resolution Molecular Dynamics Simulation (AdResS): Changing the Degrees of Freedom on the Fly

Physical Chemistry Laboratory I CHEM 445 Experiment 6 Vapor Pressure of a Pure Liquid (Revised, 01/09/06)

molecular aggregates would then be present in the water: e.g., linear chains containing

IDEAL AND NON-IDEAL GASES

Differential Relations for Fluid Flow. Acceleration field of a fluid. The differential equation of mass conservation

A R C H I V E S O F M E T A L L U R G Y A N D M A T E R I A L S Volume Issue 2 DOI: /v

Convection in water (an almost-incompressible fluid)

HEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi

Lecture 3 Fluid Dynamics and Balance Equa6ons for Reac6ng Flows

Probability and Random Variables. Generation of random variables (r.v.)

Chapter 5: Diffusion. 5.1 Steady-State Diffusion

Mathematical Modeling and Engineering Problem Solving

k L a measurement in bioreactors

In order to solve this problem it is first necessary to use Equation 5.5: x 2 Dt. = 1 erf. = 1.30, and x = 2 mm = m. Thus,

Problem Set MIT Professor Gerbrand Ceder Fall 2003

CHAPTER 14 THE CLAUSIUS-CLAPEYRON EQUATION

Flow characteristics of microchannel melts during injection molding of microstructure medical components

Fundamentals of THERMAL-FLUID SCIENCES

Alloys & Their Phase Diagrams

Igneous Geochemistry. What is magma? What is polymerization? Average compositions (% by weight) and liquidus temperatures of different magmas

The Second Law of Thermodynamics

Exergy Analysis of a Water Heat Storage Tank

PLASTIC REGION BOLT TIGHTENING CONTROLLED BY ACOUSTIC EMISSION MONITORING

Chapter Outline Dislocations and Strengthening Mechanisms

Ultrasonic Detection Algorithm Research on the Damage Depth of Concrete after Fire Jiangtao Yu 1,a, Yuan Liu 1,b, Zhoudao Lu 1,c, Peng Zhao 2,d

Experiment 5: Phase diagram for a three-component system (Dated: April 12, 2010)

Thermal transport in the anisotropic Heisenberg chain with S = 1/2 and nearest-neighbor interactions

ME6130 An introduction to CFD 1-1

Transcription:

PHASE-FIELD MODELING OF CONTACT MELTING IN BINARY ALLOYS Kartuzov V.V. 1, Bystrenko O.V. 1, 1 Frantsevich Institute for material sсience problems, Kiev, Ukraine Bogolyubov Institute for theoretical physics, Kiev, Ukraine Abstract. Computer simulations of the phenomenon of contact melting in binary alloys with chemical miscibility gap are performed on the basis of the phase field theory. Kinetics of the process is examined within the isothermal approximation, as a function of initial state. As evidenced by simulations, the simplest phase field model is capable of reproducing the basic properties of the phenomenon. The numerical results obtained suggest the diffusive nature of contact melting. Key words: phase field theory, eutectic melting, miscibility gap. 1. Introduction. The goal of this work is a study of the phenomenon of contact melting (CM) characteristic of binary systems with chemical miscibility gap in solid state. Its essence is that the two solid components of a binary alloy, being separately in equilibrium at a temperature below both melting points, but above the minimum melting temperature, start melting when brought into contact. In spite of the fact that CM is rather common in multicomponent systems and has important industrial implications [1], its theoretical explanation is till now mainly limited to general thermodynamical considerations ignoring the kinetics of the phenomenon. To investigate CM in more detail, we employ computer simulations based on the phasefield theory (PFT), which received in recent years wide acceptance as a tool for description and numerical simulation of processes of structure- and phase formation in various materials [-4]. PFT is based on the idea to describe the properties of complex systems in terms of continuous phase variables, which specify the phase state (liquid or solid) as well as any other properties of media. This makes possible to approximate the sharp interfaces between the phases by transition layers and avoid the complications associated with solving free boundary problems. To describe the microstructural evolution of a material, the dissipative dynamics equations for the phase fields, temperature and concentration are employed. It should be mentioned that the vast majority of works reporting PFT-based simulations (see, for instance, [-7])are mainly dealing with the formation of various patterns in materials, while the above mentioned phenomenon of CM remains poorly examined. In this work we use the simplest version of PFT for binary alloys, where the specific kind of phase diagram is provided by the chemical miscibility gap of solid components. In spite of limitations in the description of differences in solid phases and solid-solid interfaces [8], it still reproduces a number of basic properties of such alloys, and may provide a basis for important conclusions.. Basic PFT equations. PFT is based upon the fundamental principles of irreversible thermodynamics. In particular, in order to study isothermal processes in binary systems, we can start with the free energy representation of a system in the form of the functional of phase variables and concentration εc εφ F = [ f (φ, c,t ) ( c ) ( φ ) ] dv (1) where f ( φ, c,t ) is the free energy density; Т, c, and φ denote the temperature, concentration and the phase field, respectively. Then, by applying the fundamental requirement of thermodynamics that the free energy can only decrease in an isothermal process, one arrives at the PFT equations describing the dissipative microstructural dynamics in complex media. For the particular case of an isothermal binary system consisting of A and B components, they read [4] f φ = M Φ εφ φ t φ ()

c f = M C c (1 c ) ε C c (3) t c Here the quantities M Φ and M C are the kinetic coefficients specifying the relaxation rate of the system to the equilibrium state; εφ and εc are the model parameters, which determine the surface energy for interfaces and introduce into the model the dependence on the concentration and phase gradients; and the component concentrations c A and c B are related to the concentration c as c A = 1 c ; c B = c. The meaning of the phase variable is that it specifies the phase state, φ = 0 for solid, and φ =1 for liquid, at the point (x,t). The specific features of the microstructural processes in the system are determined by the particular form of free energy density f (φ, c,t ). In what follows, we use its classical expression for a non-ideal binary system [4] f (φ, c, T ) = (1 c ) f A (φ, T ) + cf B (φ, T ) + [ + c (1 c ) ΩS [1 p (φ)] + ΩL p (φ) ] RT νm [c ln c + (1 c ) ln(1 c )] (4) where R is the gas constant, νm is the molar volume, ΩS and ΩL are the mixing energies for the solid and liquid state, respectively. The component free energies f A (φ, T ) and f B (φ, T ) have the form T A, B T f A, B (φ, T ) = W A, B g (φ ) + L A, B M A, B p (φ ) (5) TM where TMA and TMB are the melting temperatures, W A and W B are the energetic barriers associated with the surface energy of liquid-solid interfaces for the components A and B; L A and LB are the component latent heats; the functions g (φ) = φ (1 φ) and p (φ) = φ 3 (10 15φ + 6φ ) are the barrier and interpolating functions constructed in such a manner as to provide the description of the liquid-solid interfaces of a finite width. The kinetic coefficients M Φ and M C are determined for a binary system as M Φ = (1 c) M A + cm B (6) D + p (φ )( D L DS ) MC = S (7) RT /ν m with DS and D L being the solid and liquid diffusivities, respectively. 3. PFT modeling of CM. Numerical Results. To examine the process of CM in a binary system within the isothermal approximation, the system of Eqs.(-3) was solved numerically, in 1D and D geometry, for the following set of model parameters: domain of solution was X max =.0 10 4 cm; time interval for solution of non-steady problem t=0 5 sec; difference in the mixing energies for solid and liquid phases Ω = 3500 J/cm 3 ; melting temperatures TMA = 3500 and TMB =3000 К; latent heats LA = 4500 and LB = 1000 J/cm 3 ; surface energies for liquid/solid interfaces σ A = σ B = 3 10 5 J/cm ; kinetic parameters for interfaces µ A = 0.5 cm/( K sec) ; µb = 0.1 cm/( K sec) ; diffusivities DS = 10 8 сm /sec and DL = 10 5 сm /sec. We give below the results of simulations in the dimensionless form, by using the basic units defined as follows. As the length unit l 0 we take the size of solution domain, for the time unit we use the typical diffusive time t 0 =l 0 / D S ; the quantities with the dimensionality of specific energy like f (φ, c, T ), Ω, W A, B and L A, B are measured in the units of f 0 = RTMA /ν m, and the temperature unit is TMA. Further dimensionless quantities (marked with overline) entering the basic PFT equations are defined as DL DL / DS ; M A, B M A, B f 0 t 0 ; εφ,c εφ,c /(l 0 f 0 ). Accordingly, in dimensionless form the relevant parameters used in PFT-simulations were: TMB =0.86 ( TMA 1 ); L A =1.15, LB =0.5; Ω =0.89; D L = 10 3 ( DS 1 ); W A = WB =.3 10 3 ; M A = 10 8 ; M B = 7.8 10 7 ; ε Φ = 1.15 10 5 ; ε C = 1.15 10 4.

Let us say a few words about the choice of parameters. Most of them are within the range typical for real materials and similar PFT simulations. The estimation of the concentration gradient coefficient εc from the experimental data seems to be impractical. We assumed its square to be by an order greater than that of phase gradient coefficient εφ, because the solid-solid surface energy is typically greater than that of solid-liquid interface, and the above coefficients are responsible for these interfacial energies. In evaluating the parameters needed for simulations, we used the relations given in Ref.[4] between the barrier W A, B and surface σa, B energies, respectively, as well as those for the kinetic parameters µa, B and M A, B. To examine the processes of CM, the relevant phase diagram with melting lines is needed. Conventionally, these can be obtained from the requirement that the chemical potential must be constant at solid-liquid interface [4]. Here we compute the phase diagram numerically, in a straightforward manner. For this purpose, PFT equations (-3) were repeatedly solved with different initial conditions corresponding to high density set of points on the (T,c) plane in the vicinity of melting lines, and the final equilibrium solutions were used to identify the associated (solid, liquid, or mixed) phase state. The results for the above parameters are given in Fig.1. In numerical simulations of CM Eqs.(-3) were solved for the given constant temperature T = 0.75 above the minimum melting temperature TE = 0.61 on the phase diagram, and below the melting temperatures TMB =0.86 and TMA 1 of both components. The initial concentration distribution has been set in such a way as to describe two pure components (c=0 and c=1) in solid state separated by some transition region (of the width 0.05 ), where c varies from 0 to 1 (Fig., right). Notice, that at the temperature T = 0.75 the points c=0 or c=1 specify the thermodynamically stable solid phases of pure components. It should be pointed out, that in the absence of fluctuations the phenomenon of CM is not observed due to the fact that the PFT equations by themselves allow an infinite existence of steady solutions describing the overheated solid state. The usual way to treat this problem is to add the Gaussian noise terms responsible for fluctuations to PFT equations [9-11]. Unfortunately, the accurate description of dynamical fluctuations in PFT-formalism seems to be yet not solved theoretical problem (see, for instance, the comments on closely related issues in Refs. [1-13] and the references therein). For this reason, to trigger the process of CM, we introduced small additional noise with 0.01 mean-square deviation to the initial phase distribution ( φ = 0 ) only. It is to mention that the amplitude of the initial noise considerably affects the initial starting time point, but not the kinetics (i.e., rate, typical behavior, etc.) of the CM process itself. c φ = 0 x =0, X max ; = 0 x =0, X max. The boundary conditions used in simulations were x x A number of computer runs with different initial conditions has been performed: a) 1D simulations for the average concentration c = 0.5 with the corresponding point Q in the liquid area on the phase diagram (Fig.3); b) 1D simulations for the average concentration c = 0. with excess of one of the components and with the corresponding point P in the solid area on the phase diagram (Fig.4); c) 1D simulations for the average concentration c = 0.36 with the corresponding point R located in the area of liquid-solid coexistence (Fig.5); d) D simulations for the average concentration c = 0.5 (Fig.6). As is evidenced by the results obtained, the simulations reproduce the general features of CM; the latter manifests itself by the formation of quickly growing liquid area with φ =1 (Figs.3-6). The short initial stage in all the cases is quite similar, while the final state of a system depends on the initial conditions used. In the case a), as one would expect, the complete melting of both components in the end is observed. In case b), the phenomenon of CM is observed as well, however, the diffusion processes give rise to equalization of the overall concentration resulting in the re-crystallization of the alloy into the final solid state with the concentration corresponding to the point P ( c = 0. ). In the case c), the final state turns out to be a mixture of solid and liquid of intermediate concentrations (c=0. and 0.44) indicating that the point R belongs to the area of solid-liquid coexistence. In Fig.1, this area, bounded by the solidus and liquidus lines, is filled in grey. Results of D simulations correlate well with 1D case; however, as is seen from the figure, due to the effects of random noise, the process of CM starts non-simultaneously at different boundary points, which results in the irregularity of the liquid layer between the components. The distinguishing common

feature of the kinetics of CM in all cases is a very short time of formation of liquid layer at initial stage, by orders less than the typical diffusive time t 0 = l 0 / DS used as the unit in simulations. 4. Conclusions To conclude, the computer simulations performed have demonstrated the capability of the simplest PFT version with chemical miscibility gap to reproduce the basic properties of CM in binary alloys. After the very short initial stage associated with the formation of liquid layer between the solid components, the melting proceeds to a steady state, which depends on the parameters, phase diagram and initial state of the system. The results obtained suggest the diffusive nature of contact melting, since the latter is observed within the isothermal approximation. Acknowledgements The authors acknowledge the support of EOARD, Project No 118003 (STCU Project P-510). References 1. Zalkin V M 1987 Nature of Eutectic Alloys and Effect of Contact Melting (Moscow: Metallurgiya).. Singer-Loginova I, Singer H M 008 Rep. Prog. Phys. 71 106501. 3. Chen L Q 00 Ann. Rev. Mater. Res. 3 113 140. 4. Boettinger W J, Warren J A, Beckermann C and Karma A 00 Annu. Rev. Mater. Res. 3 163. 5. Apel M, Boettger B, Diepers H J, Steinbach I 00 J. of Crystal Growth 37 39 154 158. 6. Nestler B, Wheeler A A 00 Computer Physics Communications 147 30 33. 7. Lewis D, Pusztai T, Gránásy L, Warren J and Boettinger W 004 JOM April 34-39. 8. Wheeler A A, Mc Fadden G B and Boettinger W J 1996 Proc. R. Soc. Lond. 45 495-55 (no. 1946). 9. Elder K R, Provatas N, Berry J, Stefanovic P and Grant M 007 Phys. Rev. B75 064107. 10. Drolet F, Elder K R, Grant M and Kosterlitz J M 000 Phys.Rev. E61 6705. 11. Karma A and Rappel W J 1999 Phys. Rev. E60 3614. 1. Van Teeffelen S, Backofen R, Voigt A and Löwen H 009 Phys. Rev. E79 051404. 13. Marconi U M B and Tarazona P 1999 J. Chem. Phys. 110 803.

Figures B A Fig.1. Phase diagram for a binary system obtained from PFT equations for T M =0.86 ( T M 1 ); L A =0.89. Liquid-solid coexistence area is filled in grey. =1.15 and L B =0.5; Ω Fig.. Typical initial distributions for the phase (left) and concentration (right). The initial distribution of phase variable corresponds to the solid state φ=0 with 0.01-amplitude noise.

Fig.3. Kinetics of CM process for the average concentration c =0. 5 (point Q) ; the phase (left) and concentration (right) curves are given for the time points 6 6 5 4 t=1. 7 10 (1);.3 10 ( ) ;. 0 10 (3 ) ; 3. 0 10 (4 ); 1. 0(5 ). In the end, the complete melting ( ϕ=1 ) is observed in the system.. Fig.4. Phase (left) and concentration (right) evolution in the process of CM for the average concentration c =0. (point P) for the time points t=. 0 10 6 ( 1) ; 3. 3 10 5 ( ); 5. 0 10 4 ( 3 ) ; 0. 4( 4); 1. 0( 5 ). In the end, the complete re-solidification ( ϕ=0 ) of the melt formed in the process of CM is observed.

Fig.5. Phase (left) and concentration (right) evolution in the process of CM for the average concentration c =0. 36 (point R) for the time points t=1. 7 10 6 ( 1) ; 3. 3 10 5 () ; 1. 0 10 3 ( 3); 1. 0( 4). In the final state, the co-existence of solid ( ϕ=0 at c=0. ) and liquid ( ϕ=1 at c=0. 44 ) is observed. Fig.6. Results of D PFT simulation of CM for the average concentration c =0. 5 (point Q). Evolution of phase (top) and concentration (bottom) distributions on the unit square for t=0 ;. 0 10 6 ; 4. 0 10 6.