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The attached paper gives a description of a multi-phase KKS model. We have implemented the switching functions they use in Eq. 10 for a different project. The kernel is in the phase-field module and is called ACSwitching and it gives the derivative of that switching function with respect to a particular order parameter. I haven't looked at this paper in detail in a little while, but I think there are some changes in the Cahn-Hilliard equation implementation that would need to happen too.Please let us know how this progresses for you, a multi-phase KKS model is something we would be interested in having in the framework so we would be willing to work with you to implement it and and incorporate your changes into the framework.
On Fri, Apr 28, 2017 at 9:50 AM, Johan Hektor <johan....@gmail.com> wrote:
Hi,I've just started implementing a KKS type phase field model for simulating growth of intermetallic compounds in the Cu-Sn system (see attached paper) in Moose. I want to use one order parameter for each grain of each phase. I've found the file kks_multiphase.i which is a KKS model with 3 order parameters. What would be a reasonable approach for extending that file to N-order parmeters? From what I understand the kernels (e.g. KKSMultiACBulkC) are written in general way, but the switching function is not. If I write an appropriate switching function, can I add more order parameters to my simulation just by copy+paste in the input file?CheersJohan Hektor
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When you say you need 2 concentrations- are you looking at a two-species or three-species system? I'm assuming you mean three total species with two concentrations needed to represent two solute species but just wanted to confirm first before answering. What are the chemical species and phases?
Yes it’s a 3 species film system: iron | iron-oxide | iron-sulfide | environment
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There's a couple of different routes you could go. You could use the existing 3-phase KKS model and add an additional concenration variable. The three-phase KKS model is described in
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I have tried this and it did seem to work OK. However to make sure, I would start with a binary system at a temperature between the solidus and liquidus, plot both free energies and use the common tangent construction to get the equilibrium compositions. Then simulate a two-phase system and make sure that when the system reaches equilibrium, the equilibrium compositions in the model match the compositions predicted by the common tangent construction.