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Viscoelastic Fluid Flows using OpenFOAM The solver viscoelasticFluidFoam |
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May 16, 2009, 14:57 |
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#21 |
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Kerstin Heinen
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Hi,
Oh sorry, I didn't read correctly... viscoplastic makes sense for this equation... I am still confused. In pricipal your equations don't look very difficult because explicit. But your .doc files are not self explaining... your epsilon with "overline and dot" is a scalar elongation rate? Calculated e.g. from trace of D tensor? or is this something else? and in the first equation, still I don't get the meaning of "d"... "D" is clear. \tau is a tensor... and D is a tensor...but what is deviator? I am really interested in understanding this approach. Looks for me in principal as a extension of newtonian stress tensor law with non constant viscosity. And viscostity is a function of temperature and shear rate... Can you give a literature reference for the first equation? Kerstin |
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May 17, 2009, 12:10 |
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#22 |
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xianghong wu
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Hi,
they are two different model. d means deviator, I don't know exactly what does it mean also. I will check later. the first is coming from the thesis of Proefschirift: finite element simulation of the aluminum extrusion process. the author uses it according to: L.A. Lalli and A. J. DeArdo. Experimental assessment of stucture and property prediction s during hot working. and R.N.Wright , G.G.Lea, and F.F.Kraft. Constitutive equations and flow stress characterization concepts for aluminum extrusion. the second is coming from the software Superforge. thank you Wendy |
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May 18, 2009, 19:47 |
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#23 |
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xianghong wu
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Hi,
I did the details for the first model. please see the attachment . Please check if it is correct. as for the second model I will do it right after. Thank you. Wendy |
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May 19, 2009, 13:27 |
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#24 |
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Kerstin Heinen
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Hi,
ah ok. D^d is dyadic product... in OpenFOAM nomenclature it is D && D But still your equation is then not very universal. D : D is a scalar quantity. So your stress tau is also scalar, because you multiply scalar viscosity with D^d... If you like to include the new stress _tensor_ in the momentum balance, you need a tensor equation for your material law. tau= 2 eta(D,T) D^d is a scalar equation. I would guess you mean tensor tau = 2 eta(shearrate, temperature) D and D is also tensor...but in principle you have only explicit equations and you need to update the calculation of viscosity in each iteration step with actual values of shearrate and temperature. define the shearrate e.g. like volScalarField shearrate ( IOobject ( "shearrate", runTime.timeName(), mesh, IOobject::NO_READ ), pow(2.0/3.0* (Dtensor && Dtensor), 0.5) ); define Z and eta similar and update calculation of Z and eta in the time loop.... |
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May 19, 2009, 17:25 |
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#25 |
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xianghong wu
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Hi,
Thank you for your reply. Do you mean D^d is equal to D? Then tau is a scalar? Thanks. Wendy |
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May 19, 2009, 17:26 |
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#26 |
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xianghong wu
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Sorry, I typed D : D
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May 19, 2009, 17:32 |
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#27 |
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xianghong wu
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I guess you are right, I agree with that tau= 2 eta( D,T) D. tau is a tensor
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May 19, 2009, 22:06 |
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#28 | |
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MrFluent
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Quote:
is the gamma dot that you have written is shear rate. you wrote gamma dot = sqrt( (2 /3) D : D) I think if your gamma dot is shear rate than the above expression is wrong as shear rate should be : shear rate = sqrt( 2 D : D ). I mean this is how i used it for power law fluid in my solver. |
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May 20, 2009, 00:48 |
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#29 |
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xianghong wu
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I don't know if it is wrong or not, I copied it from a PhD thesis of B.J.E. van Rens.
Thank you. Wendy |
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May 20, 2009, 02:44 |
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#30 |
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Kerstin Heinen
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May 20, 2009, 11:56 |
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#31 |
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xianghong wu
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Sorry, I did not mean that.
I only has not finish D^d equation because I was not sure how to do it. Now please see the attachment for the equation of D^d Thank you very much. Wendy |
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May 20, 2009, 12:01 |
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#32 |
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xianghong wu
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forgot to attach it. Sorry.
Wendy |
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May 20, 2009, 12:32 |
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#33 |
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Hello Andy,
This seems confused. What you need to have is the correct formulation for each term of your model (mainly for D^d)!! I think you get it where this model was introduced!! The gamma dot can be defined in different ways, the more used is shearRate = sqrt( 2 D : D ), but see what is correct in the definition of your model. I believe tau=2eta(D,T)D, where D is a tensor obviously (tau is a tensor!!!!) or D^d is the deviatoric part of D, but still is a tensor!! Then after you have the correct formulation, follow icoFoam solver: 1) create the temperature T (volScalarField) like the pressure p in icoFoam; Info<< "Reading field T\n" << endl; volScalarField T ( IOobject ( "T", runTime.timeName(), mesh, IOobject::MUST_READ, IOobject::AUTO_WRITE ), mesh ); 2) Read all the properties for your model like for nu: dimensionedScalar nu ( transportProperties.lookup("nu") ); 3) Put your T equation into the time loop, before or after UEqn?? follow your algorithm, if before: fvScalarMatrix TEqn ( the equation ); 4) Update you viscosity, using your model like for Carreau-Yassuda, for example: volScalarField etaEff = eta0 * Foam:ow( 1 + Foam:ow( K* sqrt(2.0)*mag(symm(fvc::grad(U))),a), (m - 1)/a ); here sqrt(2.0)*mag(symm(fvc::grad(U))) = sqrt( 2 D : D ), if is sqrt( 2/3 D : D ), no problem, do this modification!! 5) Use etaEff into your moment equation 6) Enjoy Jovani |
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May 20, 2009, 12:49 |
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#34 |
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xianghong wu
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Hi, Jovani,
Thank you very much. I now understand that D^d is a deviative part of D. it is a tensor, tau is a tensor, yes. I will study your code right now. I am really a beginner. I will ask you when I have questions about it. Thank you very much, I really appreciate that. Wendy |
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May 20, 2009, 14:01 |
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#35 |
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Hello Wendy,
Sorry for "Andy" in my last post!! Another suggestions for you: You can obtain the deviatoric part of a tensor directally in the OpenFoam, for example, if you have a tensor T the function dev(T) give to you the deviatoric of this tensor, see page 21 and 24 of the programer's guide! Have a good job, Jovani |
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May 20, 2009, 19:57 |
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#36 |
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xianghong wu
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Hi, Jovani,
It is really a good suggestion for me. And I know you are talking to me. so never mind. Thank you very much. Have a nice day. Wendy |
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May 20, 2009, 22:08 |
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#37 |
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xianghong wu
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Hi, Jovani,
When you mentioned programmer's guide, do you mean the webpage? http://www.nabla.co.uk/ or is there another document? I can not see page number on the programmer's guide Thank you. Wendy |
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May 20, 2009, 22:19 |
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#38 |
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xianghong wu
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Hi, Jovani,
I found the PDF document of programmer's guide. Sorry for disturbing again. Wendy |
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May 21, 2009, 23:49 |
the way I changed the constitutive model to viscoplastic
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#39 |
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xianghong wu
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Hi, Jovani,
Thank you for your help (and Kerstin also ) , I have done the modification based on icoFoam slover to solve viscoplastic problem. the attachment is the steps I did. would you have some time to see if it is right or not? thanks again. Have a nice weekend. Wendy |
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May 21, 2009, 23:50 |
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#40 |
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xianghong wu
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Sorry , I can not upload it.
so just paste here 1 ) set up viscoPlasticProperties file FoamFile { version 2.0; format ascii; class dictionary; object viscoPlasticProperties; } // modified based on viscoelasticProperties // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // //InnerIterations 1; //Solver Algorithm control //nuS nuS [0 2 -1 0 0 0 0] 1e-5; rho rho [1 -3 0 0 0 0 0] 2700; //numberOfModes 3; R [0 0 0 -1 0 0 0] 8.321 // J mol^-1 K^-1 A [0 0 -1 0 0 0 0]1.445e+12 n 4.750 beta [-1 1 -2 0 0 0 0] 3.224e-8 deltaH 1.772e+5 // PTTExp on; //PTTExp on, off; // PTTLin off;//;on; //PTTLin on, off;4.750 // ************************************************** *********************** // 2) read the properties in createFieldPlastic.H Info<< "Reading viscoPlasticProperties\n" << endl; IOdictionary viscoPlasticProperties ( IOobject ( "viscoPlasticProperties", runTime.constant(), mesh, IOobject::MUST_READ, IOobject::NO_WRITE ) ); dimensionedScalar rho ( viscoPlasticProperties.lookup("rho") ); dimensionedScalar R ( viscoPlasticProperties.lookup("R") ); dimensionedScalar A ( viscoPlasticProperties.lookup("A") ); dimensionedScalar beta ( viscoPlasticProperties.lookup("beta") ); Scalar deltaH ( readScalar(viscoPlasticProperties.lookup("deltaH") ) ); scalar n ( readScalar(viscoPlasticProperties.lookup("n")) ); //effective shear rate volScalarField etaEff ( IOobject ( "etaEff", runTime.timeName(), mesh, IOobject::NO_READ, IOobject::NO_WRITE //why ), sqrt(2.0/3)*mag(symm(fvc::grad(u))); // ); volScalarField Z ( IOobject ( "Z", runTime.timeName(), mesh, IOobject::NO_READ, IOobject::NO_WRITE ), etaEff*exp(deltaH/(R*T)); // Zener-Hollomon parameter ); // viscosity volScalarField eta ( IOobject ( "eta", runTime.timeName(), mesh, IOobject::NO_READ, IOobject::NO_WRITE ), asinh(pow(Z/A,1.0/n))/(3*beta*etaEff); // viscosity ); //dynamic viscosity volScalarField eta_d ( IOobject ( "eta_d", runTime.timeName(), mesh, IOobject::NO_READ, IOobject::NO_WRITE ), eta/rho; //dynamic viscosity ); 3) my_icoFoam_viscoPlastic.C Info<< "\nStarting time loop\n" << endl; for (runTime++; !runTime.end(); runTime++) { Info<< "Time = " << runTime.timeName() << nl << endl; # include "readPISOControls.H" # include "CourantNo.H" // here add viscosity calculation etaEff=sqrt(2.0/3)*mag(symm(fvc::grad(u))); Z=etaEff*exp(deltaH/(R*T)); eta=asinh(pow(Z/A,1.0/n))/(3*beta*etaEff); eta_d=eta/rho; // end of adding fvVectorMatrix UEqn ( fvm::ddt(U) + fvm::div(phi, U) - fvm::laplacian(eta_d, U) // right?? change nu to eta_d ); ........................... // and add T field calculation fvScalarMatrix TEqn ( fvm::ddt(T) +fvm::div(phi,T) -fvm::laplacian(DT,T) ); TEqn.solve(); runTime.write(); Info<< "ExecutionTime = " << runTime.elapsedCpuTime() << " s" << " ClockTime = " << runTime.elapsedClockTime() << " s" << nl << endl; |
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