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January 8, 2013, 19:33 
Species Conservation at Solver Level

#41 
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Chris
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Firstly, thanks everyone who contributed to this thread, it's been very helpful with my development.
The issue I'm having is that I would like to handle the species conservation equation at the solver level (not use mstm().correct() ) for a variety of reasons. I'd like to use diffusion coefficients from the Maxwell Stefan mass transport model and Chapman Enskogg binary diffusion coefficients. From what I've managed to figure out I'm going to need to be able to assign a variable to my diffusion coefficients and be able to call updatecoefficients() from the mass transport model (maxwell steffan in this case). It's easy enough to say but I've had little luck, I think I have pulling the diffusion coefficients up to my solver from the mass transport model done properly but I can't seem to figure out how to call updatecoefficients(). I feel like this is a really simple thing to program with only minor changes to the code but I'm stuck as to what to do. What I've tried is adding the function declaration for updateMolarFractions() (void updateMolarFractions(); ) to the multispeciestransportmodel header file and then calling updateMolarFractions using mstm().updateMolarFractions() (the mstm() implementation is the same as in the modified reacting foam). This compiles with /wmake libso but when i go to make the application with /wmake I get the following error: undefined reference to `Foam::multiSpeciesTransportModel::updateCoefficie nts()' Like I said, I feel this is simple and I'm just missing something basic. Edit: managed to get it to solve for the maxwell coefficients at the solver level using the mstm pointer for the Dij information. I would still be interested to see if there's a more eloquent solution out there though. Last edited by ChrisA; January 9, 2013 at 20:51. Reason: Further details 

February 26, 2013, 11:25 

#42  
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Olivier
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Hello mhsn,
Quote:
regards, olivier 

February 26, 2013, 11:44 

#43 
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Mhsn
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Olivier, I couldn't attach the files here. If you give me your email, I can email you the modified files.


February 27, 2013, 03:06 

#44 
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Olivier
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hello,
Thanks mhsn , Valerio, and Co ..... I put the 2.1.x version here if other people want it. regards, olivier 

March 13, 2013, 04:59 

#45 
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Lei Deng
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hello everyone,
i am now using also this multispeciesLibary (champanEnskog+ Fick) in OpenFoam2.1.0 . i simulated a One Dimensional premixed laminar flame with reduced mechanisms (methane oxidation, 15 species, 21 reactions) in OpenFoam, and got two problems when I compared the results with cantera and original reactingFoam. 1. temperature does not match 2. production (H2O, CO2) does not match The operating conditions and boundary conditions in cantera and openfoam are same. i already compared all coefficient in OpenFoam and cantera, such as mixture diffusion coefficient, thermoal conductivity, viscosity, ... They are all same. I also directly replace the term fvm::lapacian(D_[i], yi) with the unity lewis Nr. term fvm::laplacian(turbulence.muEff(), yi) in the subclass Fick.C, and remove mass diffusion term in hs equation, the it performs just like reactingFoam. It proved that, the connection between this multispeciesLibary and themoPhysical packet in Openfoam is fine. I am wondering the mixture mass diffusion coefficient may break the species conservation equation. I really appreciate that anyone who are using this library can share your experiences with me. I checked the boundary condition at the inlet used in cantera for burner stabilized flame, there is a massflux balance boundary condition (tau_i = y_i +j_i/phi) . I think i need to apply such boundary condition in OpenFoam. i will try mix of fixed value + fixed Gradient. Last edited by ldeng; March 14, 2013 at 04:01. 

March 15, 2013, 08:36 

#46 
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Olivier
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hello,
I think you are right. There is a common issue with inlet diffusion: the total flux is not only convective , but also diffusive, so if you set a fixedValue for a concentration, whit a know velocity, you will be wrong with your species flux calculation. Take a look at this thread: http://www.cfdonline.com/Forums/ope...chemistry.html So try to set diffusivity to 0 at inlet, or set a mixed condition. P.S: if you could set up a mixed condition for this, fell free to share ! regards, olivier 

March 22, 2013, 13:13 

#47 
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Chris
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Not sure if this will help, but I've managed to get around the "extra" mass due to diffusion at an inlet by correcting the inflow conditions for the mass diffusion.
I simply found the difference between my expected mass flow rate and the mass flow rate that openfoam gave me (done by integrating rho*U* inlet species concentration over a slice). We know that the difference is due to diffusion so if we assume the mass flow due to diffusion is a constant correct the inflow for that difference we arrive at a better mass flow rate. It won't be exact as the diffusion will change slightly as you change the concentration by changing the inflow velocity.. but with a few iterations you could conceivably approach the correct inflow mass flow rate. This of course only works for specific conditions where you can assume and calculate the necessary values... and isn't ideal because it potentially requires iterative simulations... but its working for my research and might be applicable to a few other people's cases. 

March 23, 2013, 06:12 

#48 
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Olivier
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hello Chris,
Yes your method should work, but is case specific. You should also take care at outlet, if you use inletOutlet condition: I've found that we can have local backflow over some face, which then lead to diffusive flux. The solution is to use zeroGradient, not inletOutlet. regards, olivier 

April 9, 2013, 23:18 
diffusivity for species themselves?

#49 
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何刚
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In the file diffusivity.C:
void Foam::diffusivity::update() { for(label i=0;i=species_.size();i++) { for(label j=i;j<species_.size();j++) { label k=species_.size()*i+j0.5*i*(i+1); Dij_[k]=eps_/tau_*DijModels_[k].D(); } } } "j=i" means that the diffusivity is calculated for species themselves? Maybe there are something that I haven't consider? 

April 10, 2013, 16:47 

#50 
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Bruno Santos
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Greetings hg2lf,
Just to confirm: do you mean the code that is in the file "diffusivityModels/diffusivityModel/diffusivityModel.C"? (I've opened the one for 2.1.x.) More specifically this piece of code? Code:
void Foam::diffusivityModel::update() { for(label i=0; i < species_.size(); i++) { for(label j=i; j < species_.size(); j++) { label k = species_.size()*i+j0.5*i*(i+1); Dij_[k] = eps_/tau_*DijModels_[k].D(); } } }
Best regards, Bruno
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April 11, 2013, 21:41 
multiSpecies

#51 
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何刚
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Thanks,Bruno,
But I still can't understand. I need to modify this library to calculate the diffusivity for gas mixtures. So maybe the physical problem is not the same with the exist one. I'll do more work for this library, so that I could solve this problem. Best regards. hg2lf 

April 14, 2013, 10:28 

#52 
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Bruno Santos
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Hi hg2lf,
From your description, I can only guess that you need either one of the following possible solutions:
Good luck! Best regards, Bruno
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April 15, 2013, 13:48 

#53 
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Chris
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Hi hg2lf,
I can't comment on it much because I stopped using this library for my work (I'm using rhoCentralFoam so I needed a predictor step in my species equation, which this library does not allow for) but I can say that the maxwellsteffan model is a full multicomponent model (handles many gas species). Ansys FLUENT uses this model, although I'm not sure if its the same implementation as is in the library. We're also using the maxwellsteffan model for our work, although directly implemented in the solver rather than through a library. The way it works in this library (and the model in general), to my limited understanding, is that the maxwellsteffan model uses binary diffusion coefficients to build an interaction matrix and then gets a multi component diffusion coefficient from that matrix for each species by summing the relevant terms. You can specify which binary diffusion coefficient to method to use (eg. chapman enskogg) and the maxwellsteffan model (should) reduce to the binary diffusion coefficient when only 2 gases are present. Hope that helps, Chris 

April 16, 2013, 02:08 

#54 
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Anderson
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Hi Friends
I use this library for simulation laminar combustion in tube. but I have some problem: maximum temperature in simulation differ about 100k with maximum temp in Reference. for this reason mass fraction of species have difference. I read library an manual and compare equations in this library with Ref (for example: Theoretical and Numerical Simulation : Poinsot ). I found there are some difference. 1. In YEqn: we have the correction velocity that is added to convection velocity to ensure conservation of species.although this term is disappeared in library. 2 . In hsEqn: we need to add one term in hs equation. although in library two terms are added. please help me if there are any reference for this solver that speak about equation. 

April 18, 2013, 05:42 

#55 
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何刚
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Hello,
everyone, in the file Fick.C, in the function updateCoefficient(), the code like this: forAll(species(), j) { if (j != i) { tmpGamma += x_[j] / Dij(i,j); } } I think I could understand the question above. 

April 18, 2013, 05:51 
bug

#56 
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何刚
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Hello,
everyone, In the file multiSpeciesTransportModel.C, in the function updateMolarFractions(), there is a piece of code, like this: const scalarField& psiCells = thermo_.psi().internalField(); const scalarField& TCells = thermo_.T().internalField(); const scalarField& yCells = thermo_.composition().Y(i).internalField(); scalarField& xCells = x_[i].internalField(); forAll(xCells, cellI) { xCells[cellI] = yCells[cellI] * psiCells[cellI] * TCells[cellI] * R / W(i); } The code:"xells[cellI] = yCells[cellI] * psiCells[cellI] * TCells[cellI]* R / W(i);" express the idea: x=Y*(1/RT)*T*Rcom/w(i); the bug is w(i), which should be the molecular weight of the mixtures. So, I think we should modified this piece of code. 

April 18, 2013, 09:07 

#57 
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Lei Deng
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hi hg2lf,
x(i) = p(i)/p p(i) = rho(i) *R/w(i) *T p = rho/psi then x(i) = rho(i) *R/w(i) *T *psi/rho = y(i)* psi *R *T/w(i), w(i) is for pure specie so code is correct Last edited by ldeng; April 18, 2013 at 11:08. 

April 18, 2013, 13:15 

#58  
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Chris
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Quote:
For reference, reactingFoam also uses this method in it's species equations. I cannot comment too much on the heat transfer terms, in my own energy equation I'm only including the enthalpy transport term (sum of h_i*J_i, still ironing out the formulation for that myself.) Regarding references for the library and it's equations, there should be a PDF in the earlier posts describing the equations used, there's also a paper by Valerio to look at. 

April 29, 2013, 03:45 

#59 
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Lei Deng
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Hi everyone,
as a conclusion to my previous diffusion flux problem: The diffusion flux at inlet is a common issue. To avoid that we have two options: 1. specify the total flux( diffusion + convection) equals to a fixed value. it is a kind of mixture boundary condition, but difficult(my opinion) to implement into OpenFOAM. 2. close the diffusion flux(set neumann bc to zeroGradient at inlet), this is not elegant but the easiest. because i also simulated a 1D burner stabilized flame in Cantera. In order to obtain a better results specially near the inlet, I specified a fixed value to all species as an initial condition based on the simulated results. After the combustion proceeded, i change the BC of intermediate species back to zero. Anyway, by such approach, i got a nearly perfect results (see attachment) compared to Cantera. regards, lei 

May 4, 2013, 23:41 
Install script

#60 
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Ismael
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hello All,
Did anybody manage to get the install script to work for OF211 ? regards, 

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