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mixing of gases, no combustion

    • Zeska ZESKA
      Bbp_participant
      I want to simulate the following problem:
      I want to study the mixture of two gases, but without combustion. the flows are supersonic and there are a total of three inlets, two of which with oxidizer and one with fuel and the gases are not premixed with the other one. I only know their pressure, which is 6 Pa for oxidizer and 12 Pa for fuel.
      I have the following procedure: 
      Sover: Density-based, Absolute velocity formulation, steady,  2D planar, no gravity
      Energy: on
      Viscous model: Spalart-Allmaras
      Speices Model: Species Transport (Ractions (volumetic) -uncheked ; Options( diffusions)-uncheked;)
                 Mixture Properties:  Mixture species: air and h2
                 denisty: ideal-gas
                 cp- mixing law
                 thermal conductivity- constant 0.0454
                 viscosity- constant 1.72e-05
                mass diffusivity-constant dilute approx 2.88e-05
       
      Boundary conditions: 
      inlet air: pressure inlet: gauge tot. press. 600000
      supersonic/initial gauge press: 600000
      thermal: 300
      species: h2: 0
       
      inlet h2: pressure inlet: gauge tot. press. 1200000
      supersonic/initial gauge press: 1200000
      thermal: 290
      species: h2: 1
       
      outlet: gauge pressure: 100000
      thermal: 300
      species: h2: 0
       
      operating pressure: 0
       
      Solution methods: 
      Formulation: implicit
      Flux-type: roe-fds
      Spatial discretization: gradient: least squares cell based
               flow: second order upwind
               modified turbulent viscoisty: second order upwind
               pseudo time method: off
       
      Initialization: hybrid (no patch)
      Iterations steps: 10000
       
      when I run the simulation, the residuals go high (higher than e+04) and the simulation stops. 
      what have I done wrong? What do you thinnk of my procedure? Is it plausible?
    • Rob
      Forum Moderator

      Check the pressure field after the initialisation process. Also, what stops the mixing region dropping to 100,000 Pa very quickly once it's running? The pressure based coupled solver is good to about 3M so you may not need the Density based solver. 

    • Zeska ZESKA
      Bbp_participant

       

       

      Hi Rob
      Thank you very much for your reply!
      I changed the solver to pressure based and the method to Coupled. The rest is completly the same. After initialization I plotted the pressure and density contours and they looked good. The pressure and density 
      at the boundaries show the values ​​that I prescribed. 
      I run the simulation once again for 10000 time steps, but it stoped after around 900 time steps and it said that the solution converged. Do you think that's ok/normal?
      Moreover, when I plot the final pressure contour, the values at the boundaries are not the one that I had at the begging, but values that are slightly lower, like 1 or 2 bar lower. What causes that?
       
       

       

       

    • Rob
      Forum Moderator

      It shouldn't stop at 900 time steps; 900 iterations is plausible. If you go to Monitors>Advanced you can stop checking convergence and then run on. 

      Re the boundary values. Assuming the solution is converged (not just residual checks) check the mesh and also that you're looking at the correct pressure (static, total etc). 

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