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Thermodynamic data A tutorial course Session 8: Calculation of phase equilibria from critically assessed thermodynamic data Alan Dinsdale “Thermochemistry of Materials” SRC
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Outline Describe how phase diagrams can be calculated from critically assessed thermodynamic data – What are critically assessed data ? How thermodynamic data are modelled – Temperature – Composition – Pressure Databases and software Applications 2
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Why calculate phase diagrams ? Provides way to rationalise different but related sets of experimental properties..... and to extrapolate thermodynamic data from small systems into higher order systems in such a way that they allow prediction of multicomponent phase equilibria Now software and data are sufficiently robust for – monitoring and controlling industrial plant – choosing materials used in everyday household appliances – understanding the way in which mankind affects the world and the environment in which we live – devising how we can perhaps make the world a safer and better place for us and our children to live in 3
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Principles of Phase Equilibrium Calculations Experimental Data 4 G(T,P,x) Model For Each Phase Develop Parameters For SMALL Systems To Reproduce Experimental Data Database Industrial Problem Predictions For LARGE Systems Problem Solved MTDATA Validation
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In a nutshell
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Model Gibbs energy over a range of temperatures and compositions 6
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…. in order to calculate the phase diagram 7
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What are critically assessed data ?
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What do we mean by critically assessed data ? Enthalpies of mixing of liquid Cu-Fe alloys Large scatter in experimental values Which data best represent reality ?.. and are these data consistent with … 4th WRRS 25 June 2012 IoM3, London, UK 9
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…. with the experimental phase diagram 10
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…… and measured activity data 11
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What is the aim of a critical assessment ? To generate a set of reliable data or diagrams which are self consistent and represent all the available experimental data 12 Involves a critical analysis of the experimental data ….. followed by a computer based optimisation process to reduce the experimental data into a small number of model parameters ….. using rigorous theoretical basis underlying thermodynamics
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Critical analysis of experimental data Experimental data: Search and analysis – Search through standard compilations eg Hultgren, Massalski – Use a database of references to the literature eg Cheynet – Carry out a full literature search Which properties – Phase diagram information Liquidus / solidus temperatures Solubilities – Thermodynamic information enthalpies of mixing vapour pressure data emf data heat capacities Enthalpies of transformation Ab-initio calculations 13
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Obtaining model parameters Aim is to determine set of coefficients which gives best agreement with experimental data – by least-squares fitting of the thermodynamic functions to selected set of experimental and ab-initio data It is usually carried out with the assistance of a computer – Using optimisation software MTDATA optimisation module PARROT (inside ThermoCalc) LUKAS program BINGSS CHEMOPT 14
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Calculated enthalpies of mixing for liquid Fe-Cu alloys 15
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Calculated Fe-Cu phase diagram 16
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Calculated activities for Fe-Cu liquid alloys 17
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Variation of Gibbs energy of phases at fixed temperature 18
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How to model thermodynamic data need to understand how G changes with T, P and x
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Variation of Gibbs energy of phases at fixed temperature Difference in Gibbs energy between fcc and liquid Fe Difference in Gibbs energy between fcc and bcc Cu Change in Gibbs energy with composition is complex fcc phase is reference for both elements 20
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4th WRRS 25 June 2012 IoM3, London, UK 21
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Heat capacity of Sn for different phases 22 T fus = 505.078 T trs
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Enthalpy of Sn relative to 298.15 K 23 Δ fus H Δ trs H
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Entropy of phases of Sn 24
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Gibbs energy of phases of Sn relative to BCT 25 T fus T trs
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Mathematical description of Gibbs energy variation with temperature Heat capacity generally represented by 1 or more expressions of the form: – Cp = a + b T + c T 2 + d T -2 (generally obtained from experiment) With enthalpy of formation and entropies at 298.15 K (or transition enthalpies and entropies) this leads to expressions for the Gibbs energy of the form: – G = A + B T + C T ln(T) + D T 2 + ET 3 + F T -1 – (relative to some defined reference state) 26
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Magnetic materials Magnetism has a big influence on the heat capacity and therefore on the Gibbs energy Heat capacity of bcc FeGibbs energy of liquid and bcc phases of Fe relative to fcc 27
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Effect of pressure G = H – T S + P V 28
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Effect of composition on Gibbs energy Difference in Gibbs energy between fcc and liquid Fe Difference in Gibbs energy between fcc and bcc Cu Change in Gibbs energy with composition is complex Basic approach is to use a simple theory to model what we measure and then Fit any discrepancies (excess Gibbs energy) to a power series expression 29
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Simplest theory – ideal mixing Assumes that the components (elements) mix randomly without giving off or absorbing any heat and with no net volume change The mixing does result in a change in the entropy and therefore the Gibbs energy G ideal = R T [x Fe ln(x Fe ) + x Cu ln(x Cu )] 30
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Real materials – excess Gibbs energy In most cases mixing between components (elements) is accompanied by a significant heat effect which may be simple or complex The deviation from ideal behaviour may also vary with temperature leading to an “excess entropy of mixing” 31
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Overall Gibbs energy of mixing 32
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Gibbs energy of binary solutions G = x Fe G Fe + x Cu G Cu + R T [ x Fe ln(x Fe ) + x Cu ln(x Cu )] + x Cu x Fe [ a + b (x Cu -x Fe ) + c (x Cu -x Fe ) 2 + d (x Cu -x Fe ) 3 + …..] Pure component Gibbs energies Ideal contribution to Gibbs energy Excess Gibbs energy – in this case “Redlich- Kister expression” where a, b, c, d …. could be temperature dependent (in practice for Fe-Cu we may need only one or possibly two parameters) 33
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Calculated phase diagram involving two phases 34
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From binary to multicomponent Multicomponent Gibbs energy given by 36 KohlerMuggianu Toop G = Σ x i G i + R T Σ x i ln(x i ) + G excess Various models used to extrapolate excess Gibbs energy into ternary and higher order systems from data for binary systems. Extra ternary terms used if required
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Compound phases Stoichiometric phases: variation of Gibbs energy with T similar to that for phases of elements Many important compound phases are stable over ranges of homogeneity. Crystal structure indicates sublattices with preferred occupancy. – eg: sigma, mu, gamma brass Use compound energy formalism to allow mixing on different sites – Laves phases: (Cu,Mg) 2 (Cu,Mg) 1 – Interstitial solution of carbon: (Cr,Fe) 1 (C,Va) 1 – Spinels: (Fe 2+,Fe 3+ ) 1 (Fe 2+,Fe 3+ ) 2 (O 2- ) 4 37
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Gibbs energy using compound energy formalism eg (Cu,Mg) 2 (Cu,Mg) 1 Gibbs energy again has 3 contributions Pure compounds with element from each sublattice Cu:Cu, Cu:Mg, Mg:Cu, Mg:Mg Ideal mixing of elements on each sublattice Cu and Mg on first and on second sublattices Non-ideal interaction between the elements on each sublattice but with a specific element on the other sublattice – Cu,Mg:Cu Cu,Mg:Mg Cu:Cu,Mg Mg:Cu,Mg 38
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Thermodynamic databases and software
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Thermodynamic databases Two types of databases – Collections of datasets suitable for potentially diverse materials eg SGSUB, SGSOL – Application specific databases: comprehensive set of data for particular material types All databases need to be based upon a set of standards – Consistent data for the elements – Consistent models to represent thermodynamic data based (where possible) on crystallographic information 40
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Database providers Software developers – MTDATA (NPL) – ThermoCalc (TCSAB) – FactSage (GTT, Ecole Polytechnique Montreal – PANDAT (CompuTherm) – JMatPro (ThermoTech) Specialist centres eg SGTE, CEA, Tohoku, Claustal International Collaborative Projects – COST507, COST531, COST MP0602 – Superdata, III-V semiconductor project 41
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Software packages General phase diagram calculations ThermoCalc: TCSAB, Stockholm, Sweden FactSage: GTT, Herzogenrath, Germany Pandat: CompuTherm, Madison, USA MTDATA: NPL, Teddington, UK Calculation of materials properties JMatPro: Sente Software Ltd, Guildford, UK 42
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General facilities available Single calculation of phase equilibria for defined temperature, pressure and composition Calculations over a range of temperatures for fixed composition Mass of phases in equilibrium (and compositions) Partial pressures Enthalpy changes and heat capacity Transformation temperatures Phase diagram calculations (binary, ternary, isopleths, liquidus projections) Database management Assessment and optimisation capability Simple simulations (eg Scheil solidification) 43
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Applications
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Liquidus projection for solders 45
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Isopleths: Mixing electrician’s solder with lead free solder 46
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Plot of mass of phases with variation of temperature 47
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Calculated heat capacity and volume change 48
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Use of thermodynamic data to predict thermophysical properties
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Calculation of surface tension: equilibrium between bulk and surface 50
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Oxide liquid modelled as non- ideal mixture of species 51
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Calculated viscosity 52
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Engineering toolkits
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Virtual Measurement Systems Use MTDATA to calculate properties such as liquidus and solidus temperatures, enthalpy, heat capacity and density Develop and use thermodynamics as basis for modelling other thermophysical properties Simple interface - user is shielded from complexity of models Easy to export data to Excel and other software 54
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Amalgam Toolkit for compact fluorescent lamp design 55 Provide an easy to use tool for lamp design engineers Amalgam thermodynamic database + MTDATA api Automatic selection of elements and compositions for amalgams to optimise light output Light output calculations derived from calculated materials chemistry
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Relative Light Output results 56
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Final thoughts Now possible to calculate phase equilibria for a wide range of materials Rely on good quality critically assessed data compiled into comprehensive databases A number of organisations are involved in developing database Other sorts of properties can be modelled from a thermodynamic basis Engineering toolkits offer potential to bring phase diagram calculations to the non specialist 57
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