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PanEngine for Thermodynamic Calculation

In Pandat, thermodynamic calculations are all performed by PanEngine. In the CALPHAD approach the Gibbs energies of phases in an alloy system are described by different thermodynamic models such as the random substitutional solution model, the stoichiometric compound model and the CEF. In addition to these commonly used models, PanEngine can also deal with both ideal and non-ideal gases, the ionic liquid model, the associate solution model, the CEF with ionic species and the more advanced Cluster/Site Approximation (CSA).

In order to solve the phase equilibrium problem for a multi-component system, minimization of the Gibbs energy functions described with different thermodynamic models is a pre-requisite. However, due to the possible presence of multiple solutions and the complexity of the models, the algorithms available in most commercial software packages provide no guarantee of obtaining the correct solution for the general phase equilibrium problem. This situation is exaggerated if a more complicated model such as the CEF with ionic species or the CSA is used in a multi-component system. Faced with this problem, special global optimization algorithms were implemented in PanEngine with great successes. For more information, please refer to [2002Che] for discussions of this topic and [2008Cao ] for recent improvements and benchmarks of the algorithms. 

A number of examples are given as follows (diagrams from 2008Cao ).

 

Figure 1. PANDAT point calculation results of alloy 625 (a) in a list table and (b) in a grid table (customizable); an extended grid table is automatically generated by a PANDAT point calculation.

 

Figure 2. Line calculation results of alloy 718 from 1500C to 600C.

 

Figure 3. The calculated binary Ni-Al phase diagram.

 

Figure 4. The calculated isopleth for Ni-Al-Pt system with the mole fraction of Pt being fixed at 0.05.

 

Figure 5. The calculated isothermal section for Ni-Al-Ru system at 1523K compared with the experimental data.

 

Figure 6. The liquidus projection for Ni-Al-Ir system.

 

Figure 7. The calculated solidification paths for a niobium alloy (Nb-22Ti-2Hf-4Cr-3Al-16Si in at%) using PANDAT under Lever Rule and Scheil conditions.

 

   

Figure 8. The calculated binary Fe-O phase diagram.

 

Figure 9. The calculated isothermal section of Fe-Cr-O system at 1573 K.

 

Figure 10. The calculated stability diagram of Fe-Cr-O system at 1573 K.

 

PanEngine for Thermodynamic Calculation