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If you can send a description of your work by email I will be glad to assist you

Send me an email simulationworldinquries@gmail.com

Send me an email on simulationworldinquries@gmail.com

Part 1 and part 2 shows how to build the geometry. Watch this video for more information on how to employ physics and run simulation with this type of model. The physics are explained in detailed in this video I did. HOW TO MODEL LUMPED LITHIUM ION BATTERY PACK- 3D MODEL th-cam.com/video/EweVlTYWVmI/w-d-xo.html

Send me an email on simulationworldinquries@gmail.com

Send me an email for further information

HOW TO BUILD BATTERY CONFIGURATION _COMSOL SIMULATION_part2 th-cam.com/video/3HxX7cO0BC4/w-d-xo.html

I can illustrate it to you Kindly send me an email

Can you give me your email?

Bro if you send me email can you make how to test stiffness?

You just need to join the student category and then get access to the report as you need

Certainly

I can assist you with error Kindly send an email

@@Simulation_World email address?

Yes, exactly as I did in the tutorial

It’s available for members

You can apply the same procedure to module a 3D coil. Also there are different types of results you can apply for the 3D results. You can select based on the type of results you need.

Alright you can send me an email simulationworldinquries@gmail.com

Browse to the model’s Application Libraries folder and double-click the file transport_and_adsorption_parameters.txt.

Here, csTx and csTy refer to the components of the gradient restricted to the plane tangential to the boundary where the interface is defined, that is, Boundary 5. Because this boundary is parallel to the y-axis, only csTy is nonzero in this case. T is temperature

@@Simulation_World first thank you for reply. I think that the process is isothermal so the no need to take Ty or Tx, because they will =0, do you agree?

This example demonstrates how you can model different dimensions (2D and 1D in this example) in a fully coupled manner using COMSOL Multiphysics. It involves a small parallel-plate reactor with a catalytic surface. When modeling chemical reactions, the reaction rates are commonly functions of the concentrations of the reactants in the phase that transports the chemicals. Similar applications where surface processes are of critical importance include biochip devices and semiconductor components. The equations used include those for the Transport of Diluted Species interface as well as the General Form Boundary PDE interface on the active-surface boundary.

Hello, you are applying this study on your work right? Also please check in the parameters section how the C_rate is written. Next it to check if there is any input in the physics which is displayed in yellow. The error is due to a mistake in typing an expression as c_ rate I’ll recommend you start afresh if you didn’t locate this

Can send you the file on your account and can you check is its possible?

It says error in sweep

I sent you email with file please look into it

Thank you. I recommend you join our membership for exclusive tutorials Join this channel th-cam.com/channels/2J7JNsjOzLU2YXMoOaCMMw.htmljoin

Pouch cell

@@Simulation_World Is it possible to do the same internal short circuit simulation in 1d model? If yes please help!! I tried it to find the graphs and results of 1D isothermal cell (following both the 1d and 2d videos in your channel, thanks for amazing video btw 😄) by inducing a short circuit, but my results are gibberish (I don't know why 😥).

Please check the physics

I will try and let you know

Thanks

Please check the following: a) In the Settings window for Analytic, type a in the Function name text field b)Go to thermal contact 1, In the Pb text field, type -m_car*v(t)*a(t)/8.

Yes Its already there but still I m getting error

Thanks