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#1 |
Member
Akr
Join Date: Apr 2015
Location: India
Posts: 53
Rep Power: 12 ![]() |
I am trying to run a simulation using BuoyantBoussinesqPimpleFOAM.
I have re-modified the solver as a laminar transient one. In the control dict even though i have specifed maxCo has 0.5, during simulation the max courant number reaches values in the range10k-100k+ and still the simulation keeps on running. Mean courant number also varies from 0.001 to 100+ ranges. i have chosen the deltat based on the formuale (i.e. velocity/smallest cell in domain) and i am sure my mesh is a very good mesh. But ANyone know why this happens??? Any idea?? |
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#2 | ||
Retired Super Moderator
Bruno Santos
Join Date: Mar 2009
Location: Lisbon, Portugal
Posts: 10,981
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Quick question: Which OpenFOAM version are you using?
Quick answers: Quote:
Quote:
![]() In addition, if you indeed have modified the solver, then you might have broken how it adapts the time step.
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#3 |
Member
Akr
Join Date: Apr 2015
Location: India
Posts: 53
Rep Power: 12 ![]() |
Hi Bruno,
I am glad you happen to read my post ![]() So i took out, the RAS and turbulence.H files from my .C file and also from my files/options in the solver and re-complied it. Just to keep away all the unwanted aspects of turbulence in the solver. (pratically it wasnt needed but i just tried ![]() Code:
libs ( "libOpenFOAM.so" "libsimpleSwakFunctionObjects.so" "libswakFunctionObjects.so" "libgroovyBC.so" ); application Foam; startFrom startTime; startTime 0; stopAt endTime; endTime 1800; deltaT 1; writeControl timeStep; writeInterval 150; purgeWrite 0; writeFormat ascii; writePrecision 6; writeCompression off; timeFormat general; timePrecision 6; runTimeModifiable true; adjustTimeStep no; maxCo 0.5; But the results i get are somewhat in accordance with the physics of the problem. I am trying to simulate natural convection (thermosyphon effect) on tubes. In the base solver the UEqn.H is given as: Code:
fvVectorMatrix UEqn ( fvm::ddt(U) + fvm::div(phi, U) + turbulence->divDevReff(U) == fvOptions(U) ); UEqn.relax(); fvOptions.constrain(UEqn); if (pimple.momentumPredictor()) { solve ( UEqn == fvc::reconstruct ( ( - ghf*fvc::snGrad(rhok) - fvc::snGrad(p_rgh) )*mesh.magSf() ) ); fvOptions.correct(U); } Code:
// Solve the momentum equation fvVectorMatrix UEqn ( fvm::ddt(U) + fvm::div(phi, U) -fvm::laplacian(nu, U) ); UEqn.relax(); UEqn.solve(); Any Suggestions Sir ![]() Last edited by wyldckat; April 17, 2016 at 14:00. Reason: Added [CODE][/CODE] markers |
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#4 | |
Retired Super Moderator
Bruno Santos
Join Date: Mar 2009
Location: Lisbon, Portugal
Posts: 10,981
Blog Entries: 45
Rep Power: 129 ![]() ![]() ![]() ![]() ![]() ![]() |
Quick answers:
Quote:
And I'm glad I asked for the "controlDict", because these 3 entries: should be changed to something like this:
Looks OK to me. Although keep in mind that this way you can't use source terms defined with "fvOptions" for the U field. |
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#5 |
Member
Akr
Join Date: Apr 2015
Location: India
Posts: 53
Rep Power: 12 ![]() |
I was waiting even if its late at nite here f or your post
![]() ![]() Indeed yeah, I cant use my source term using fvOptions by this way. But i guess i dont need it for my problem. It seems like that. I would check with the controlDict file and let u know, what happened ![]() And about RAS properties file inside the constant directory, i removed it as i have removed RAS Header files frm .C ![]() |
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#7 |
Member
Akr
Join Date: Apr 2015
Location: India
Posts: 53
Rep Power: 12 ![]() |
Hi All,
In my problem as stated above, i am using fixedGradient to apply a uniform heat flux boundary condition on walls. Suppose I want to apply heat flux condition on the surface of a tube through which water is flowing. since i want to apply different heat flux at the top side and bottom side of the top i have written a boundary condition like topside { type fixedGradient; gradient uniform 1321.549; } bottomside { type fixedGradient; gradient uniform 320.145; } And I have set the internalfield of Temperature field to be at room temperature i.e. 298K. But when i run the simulation, the temperature on the bottom walls falls below 298K or even goes like 180K even. The temperature Equation is fvScalarMatrix TEqn ( fvm::ddt(T) + fvm::div(phi, T) - fvm::laplacian(KcEff, T) ); TEqn.relax(); TEqn.solve(); where KcEff is a dimensioned Scalar for time being. any suggestions? |
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#8 |
Member
Akr
Join Date: Apr 2015
Location: India
Posts: 53
Rep Power: 12 ![]() |
It was an error occurring due to some mistake in m pressure boundary conditions.
It works now. |
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#9 |
Member
Akr
Join Date: Apr 2015
Location: India
Posts: 53
Rep Power: 12 ![]() |
I am trying to simulate a problem similar to water flowing through a glass tube. The glass tube is provided with constant heat flux and i am using boussinesq approximation to model the natural convection taking place within the tube. The base solver i am using is buoyantBoussinesqPimpleFOAM.
The problem is transient, laminar, incompressible. I kind of modeled the problem. But i have some doubts regarding this issue. To apply a constant heat flux condition on tube walls i have used a fixedGradient Boundary condition on 0/T As we know that Q/A (heat flux) = -k* dt/dx, where k is thermal conductivity of glass Now i assume that, the water intakes the heat applied on tube walls by convection. therefore Q/A = h* (T - Tinf) If this formulation is right. I want to find out the (T-Tinf). But as i dont know much about OpenFOAM, i dont know how to compute it. I want to calculate this in every cell of the domain. Why i need (T-Tinf)? Suppose if i want to calculate the grashoffno from this solver in post processing stage. I can write the grashoff nio equation and it contains this term (T-Tinf). By finding it, i can find out grashoff no also. is it correct? If my theory is wrong, please correct me. How can i compute that (T-Tinf) from my solver? Looking forward for your help. |
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