Post-Combustion CFD simulation in rocket nozzle
Hi guys,
i am trying so simulate a species transport problem through a convergent divergent nozzle with fluent. My fluid is a mixture out of H2O(vapor), OH, H, O, H2, O2. I have the mass fraction of each specie after the combustion in a combustion chamber. I defined a reaction mechanism with 14 Reactions. (Arrhenius Rate) Ideal gas for density. Polynomial cp for every species. Pressure-Inlet:Gauge Total Pressure: 3e+6 Pa; Initial Pressure 2.9e6; total Temperatur of 3650 K Pressure Outlet: 0 Pa Operating Pressure: 0 Pa I am using a density based, axissymmetric solver with species transport, EDC reaction and k-e-turbulence model. My Problem, because im no chemical expert: The mass fractions of each specie changes drastically after the first mesh node. I have an instant jump in every mass fraction and my Temperatur jumps from ~3600K to 4700K. I think its because i have an very high inlet temperatur so the mixture is combusting after the first mesh node... but how can i produce a mixture model, which isnt combusting? I mean the combustion should take place in the combustion chamber and i want to simulate the downstream condition with the in CEA calculated mass fractions. i hope someone cann help me. if i should describe my problem more accurate plz tell me. best regards |
I am also stuck in the similar kind of problem. I want to model combustion gases through CD nozzle. I have only nozzle and external atmosphere around it in which pressure is 1000 Pa. Please help me in this regard.
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