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May 31, 2021, 07:43 |
Ethanol pyrolysis
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#1 |
New Member
Join Date: May 2021
Posts: 5
Rep Power: 5 |
Hey everyone!
I'm trying to learn how to simulate the pyrolysis process (no O2). I've created a mechanism at 1500K, 1atm using RMG (Reaction Mechanism Generator, MIT), and then reduced it using chemkin. I tried to simulate the process in fluent using species transport, importing name_gas.inp file as kinetics input (attached), and thermo.db as thermodynamic database. 3D model is a 250ml cylinder, with up and down faces as inlet and outlet. Energy- ON Viscous model- LES (tried k-epsilon too- floating point exception) Turbulence model- Eddy-Dissipation Inlet and outlet temperature- 1500K Wall temperature- 1500K Inlet species- either 100% ethanol, or 0.01 mass fraction for each species (doesn't make a difference) I run 500 iterations, at 0.01s step size. Now what happens is really interesting. A plane across the reactor shows that Ethanol FULLY decomposes into THE LAST SPECIE defined in imported materials (doesn't matter the specie, based on which specie is last in imported file- eg. c2h3o, or c#c) Chemkin post process shows a much nicer plot of time-mole fractions (attached). Now, im super new to ANSYS, so im not quite sure if i went through chemkin process right, but the .inp file seems to be fine. I'm not sure what to do, as i tried a lot of things like running the simulation in larger tank, or playing with temperature etc. Please help me to understand what am i doing wrong, as i cant seem to find a reason. |
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June 5, 2021, 08:48 |
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#2 |
New Member
Join Date: May 2021
Posts: 5
Rep Power: 5 |
Using chemkin thermodnamic database fixed the problem.
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