Ansys Assistant will be unavailable on the Learning Forum starting January 30. An upgraded version is coming soon. We apologize for any inconvenience and appreciate your patience. Stay tuned for updates.
Fluids

Fluids

Topics related to Fluent, CFX, Turbogrid and more.

DDPM-KTGF Float point error

    • gelsonrhilgemberg
      Subscriber

      Hi everyone

       

      I need help with my DDPM simulation. I am Simulating a Pilot CFB BOILER using DDPM aproach, Species Transport (finite rate-eddy dissipation) with Air-wood-volatiles. The discret phase are sand (0,3mm diameter) and biomass (1 mm). My mesh have about 5 mm and minimum ortogonal quality 0,48, avg 0,95. I am using Gidaspow for drag force and non-spherical(biomass). I run the simulation in steps (cold flow, particles, energy-species equations). When simulating reactions, the continuity residuals shows higher value in beginner of each time step and  decrease over time, however, after a few time steps after (0,2-0,5s), the solver fails in one time step with Continuity, K-omega residuals. Temperature limited in all cells, turbulent viscosity ratio too. I reduced the loop-factor, I increased the lenght time factor, the number of iterations, I Reduced the URF but without sucess. If anyone knows what can be the problem, please help me.

      Some parameters

      First Order, transient, biomass and sand have same parameters in multiphase eulerian phase tab (Granular, gidaspow, lun, schaeffer, based ktgf)

      DDPM - AIR-wood-volatiles - primary phase, sand and biomass discret phase

      K-omega SST

      Injections by surface and constant number parcell method (sand I tried 100, 50, 25 particles per parcell and biomass 1 particle per parcell)

      Boundary conditions

      air 4m/s in the bottom of riser 500k

      sand in the y tube - 0,10kg/s (in begginer 0,15kg/s, expected around 0,3-0,5 kg in the system) 873k

      air 0,5m/s in the y tube - 873k

      biomass - 0,00055 kg/s in the bottom of riser - 323k

       

       

    • Rob
      Forum Moderator

      If you switch off the reactions how does it behave? For trouble shooting you need to reduce complexity and then build back up to identify the cause. 

    • gelsonrhilgemberg
      Subscriber

      Hi

      When I Switch off the reactions the problem continues. I disabled the energy and species equation

      .

       

      My setup is this

       

      Eulerian 

      Lagrangean

       

      For sand is 25 particles, Drag force -Huilin Gidaspow (Inert)

       

      Species model

       

      Material combusting particle

      Methods are setting default.

      When I started the simulation I put just cold fluid (the residuals were good), after I injected sand particles and biomass particles and the residuals started to oscilate but in the end of the time step reached 1E-3. With the reactions and energy enabled and URF for energy and species - 0,8, the simulation run  0.1 to 0.3s with time step 1e-4 and the simulation began to diverge. When I set smaller time steps, the residuals increasing more. Any tips or adjustments that can be made?

       

Viewing 2 reply threads
  • You must be logged in to reply to this topic.
[bingo_chatbox]