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March 12, 2014, 09:41 |
Mass imbalance in fast chem. reaction
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#1 |
New Member
Alexey
Join Date: Jan 2014
Posts: 18
Rep Power: 12 |
I have a problem with chem.reaction modeling in Fluent (laminar Finite-rate model)
Boundary conditions: Mixture - 3 species Mass fraction of I0 = 0.001 Mass fraction of R0 = 0 Mass fraction of M = 0.999 Mixture flows into the tube Reactions: I0 -> 2R0 M is not involved into reaction. After calculation, mass fraction of specie I0 become 0, mass fraction of specie R0 become 0.0015, and mass fraction of M become 0.9985 (so, M turns into R0, BUT M should not react and change own mass fraction). I tried to use stiff solver, but result is the same. Any ideas? I can attach files with solution if it's necessary |
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March 13, 2014, 02:00 |
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#2 |
New Member
Alexey
Join Date: Jan 2014
Posts: 18
Rep Power: 12 |
Also one more problem.
Reaction reaction does not proceed to the end. But reagent concentration must constantly fall |
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March 14, 2014, 10:26 |
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#3 |
Senior Member
François Grégoire
Join Date: Jan 2010
Location: Canada
Posts: 392
Rep Power: 17 |
A numerical solution is not an analytical solution, there is some discrepancy depending on the numerical implementation. You get a discrepancy of 0.05% between the analytical value of Y_M and the numerical value, that's fine with me.
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March 17, 2014, 00:19 |
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#4 | |
New Member
Alexey
Join Date: Jan 2014
Posts: 18
Rep Power: 12 |
Quote:
What can be done to minimize this error? |
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