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March 24, 2021 at 8:42 am
charitra22
Subscriberi am working on fluidised bed and every time i am getting this type of problem during simulation .........please any one help me ?
March 24, 2021 at 8:47 amAitor
SubscriberCould you please give an overview of your problem? Your goal, geometry, BCs, mesh, physical models and numerical methods that are you using...The more data, the better.March 24, 2021 at 10:55 amcharitra22
Subscribermy goal is to study the hydrodynamics and temperature profile of the fluidised bed dryer ngeometry - i attached belownBC - air inlet velocity 60m/sn air inlet temp 400Kn time step size 0.01n convergence criteria 1*10^(-5)n nodes 88343n elements 462312nPhysical model - euler euler modelnsolver type- pressure based seggregated solver nturbulence model RNG k-ennear wall moodelling - standard wall functionnphase intraction model - syamlal O Brien nMarch 24, 2021 at 10:59 amAitor
SubscriberWhere is the inlet? And what about the outlet?nCould you post a screenshot of a section of the mesh? A cut with the YZ plane, for example.nMarch 24, 2021 at 11:48 amRob
Ansys EmployeeWhat's the initial particle packing set to? 60m/s may require a smaller time step too, what's the courant number in your domain? nMarch 24, 2021 at 7:00 pmMarch 24, 2021 at 7:05 pmMarch 25, 2021 at 4:55 amcharitra22
Subscriberany one ?????.March 25, 2021 at 7:28 amDrAmine
Ansys EmployeeThe mesh is really not ideal: what does Fluent tell if you issue mesh check and quality.nPlease also be more patient.nMarch 25, 2021 at 5:10 pmcharitra22
Subscriberok. I am trying to simulate dryying process also will you please help me to define wet solid in fluent and moisture content measurement.nMarch 26, 2021 at 1:51 pmRob
Ansys EmployeeYou'll need a mixture for the gas phase (air and water vapour as a guess) and a mixture for the solid, probably solid+water_liquid. Then you'll need the phase change models. That'll be more complicated. nViewing 10 reply threads- You must be logged in to reply to this topic.
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