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June 13, 2023 at 8:39 pmmehdi AbbasSubscriber
The above photo shows residual values for a transient simulation. I am confused as to why the continuity residuals are not falling . This is an enclosed box containing battery cells with time dependent heat generation and natural convection. There's an additional heater whose source values are modeled with a udf using heating table values. The step size for each Time step is 1 second. The mesh quality parameters are 0.55 max skewness and minimum orthogonal quality equal to 0.3. I am unsure why the continuity solution is not converging, I am using K omega sst viscous model. Theres no fluid entering or leaving the box and the gaps for the fluid are in millimeters.Can someone help me as to how to get this solution to converge? -
June 15, 2023 at 8:36 amMurari IyengarAnsys Employee
Can you provide more details about the Boundary Conditions as well? At the moment, it isn't very clear.Â
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June 15, 2023 at 8:41 ammehdi AbbasSubscriber
The base of the box has adiabatic boundary conditions whereas the remaining five walls have a convective boundary condition. The system is initially at room temperature.1
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June 15, 2023 at 8:40 ammehdi AbbasSubscriber
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June 15, 2023 at 8:45 amMurari IyengarAnsys Employee
You mentioned there is no fluid leaving/entering the box, then what are the gaps for? Can you share screenshots of your geometry?Â
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June 15, 2023 at 8:49 ammehdi AbbasSubscriber
This is a battery pack with cells. The volume of the box not occupied by the cells is fluid . Since the pack is closed off from the surroundings, the fluid volume doesn't change.
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June 15, 2023 at 8:52 amMurari IyengarAnsys Employee
If the fluid inside the box is present without any change in fluid flow, you can just assign convection boundary conditions to the cells. Why solve flow equation?
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June 15, 2023 at 8:54 ammehdi AbbasSubscriber
The cells lose heat to the surrounding fluid in the pack . I am trying to simulate thermal runaway propagation in a battery pack. Thus it is important to solve the flow equations
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June 16, 2023 at 1:04 pmMurari IyengarAnsys Employee
If you don't have fluid leaving/entering the domain, then your net mass flux should be 0. Is that the case?Â
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June 16, 2023 at 5:23 pmmehdi AbbasSubscriber
I haven't checked the flux . Yes it should be.
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June 16, 2023 at 1:23 pmMurari IyengarAnsys Employee
Are you using Body Force Weighted or PRESTO! as the Spatial Discretization scheme for Pressure? If not, I recommend doing so.Â
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June 16, 2023 at 5:57 pmmehdi AbbasSubscriber
Yes I am using PRESTO
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June 20, 2023 at 8:26 amMurari IyengarAnsys Employee
Can you share an image of the mesh cross section? Are the mesh cells refined near the battery cells? Apart from continuity, what do the other results look like?
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June 20, 2023 at 11:58 pmmehdi AbbasSubscriber
I did not draw boundary layersÂ
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- The topic ‘Residuals not falling in ansys fluent (transient simulation)’ is closed to new replies.
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