Aaron Dettmann
COMSOL Employee
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Posted:
9 months ago
15.07.2024, 04:56 GMT-4
Updated:
9 months ago
16.07.2024, 09:57 GMT-4
If I understand your model correctly, I believe the Enclosed Cavity feature might still be suited for solving your problem.
Note, however, that the Enclosed Cavity feature assumes that the entrapped air inside the cavity has a uniform pressure and temperature in the fluid domain, and that the gas state is governed by a global equation of state. In other words, temperature or pressure gradients cannot be resolved.
Assuming that you know the air temperature (e.g. assuming thermal equilibrium between wall and gas, or solve for a heat transfer equation), you can define your equation of state for the air (e.g. ideal gas).
You can then enter this equation of state either in the Fluid subnode, if you choose User defined from the Compressibility list. Alternatively, you could use the Prescribed Pressure subnode (and delete the Fluid subnode).
If you have any further questions, please don't hesitate to elaborate or share more details about what specifically does not work as expected.
If I understand your model correctly, I believe the Enclosed Cavity feature might still be suited for solving your problem.
Note, however, that the Enclosed Cavity feature assumes that the entrapped air inside the cavity has a uniform pressure and temperature in the fluid domain, and that the gas state is governed by a global equation of state. In other words, temperature or pressure gradients cannot be resolved.
Assuming that you know the air temperature (e.g. assuming thermal equilibrium between wall and gas, or solve for a heat transfer equation), you can define your equation of state for the air (e.g. ideal gas).
You can then enter this equation of state either in the Fluid subnode, if you choose *User defined* from the *Compressibility* list. Alternatively, you could use the *Prescribed Pressure* subnode (and delete the *Fluid* subnode).
If you have any further questions, please don't hesitate to elaborate or share more details about what specifically does not work as expected.
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Posted:
9 months ago
17.07.2024, 10:05 GMT-4
Updated:
9 months ago
17.07.2024, 20:03 GMT-4
If I understand your model correctly, I believe the Enclosed Cavity feature might still be suited for solving your problem.
Note, however, that the Enclosed Cavity feature assumes that the entrapped air inside the cavity has a uniform pressure and temperature in the fluid domain, and that the gas state is governed by a global equation of state. In other words, temperature or pressure gradients cannot be resolved.
Assuming that you know the air temperature (e.g. assuming thermal equilibrium between wall and gas, or solve for a heat transfer equation), you can define your equation of state for the air (e.g. ideal gas).
You can then enter this equation of state either in the Fluid subnode, if you choose User defined from the Compressibility list. Alternatively, you could use the Prescribed Pressure subnode (and delete the Fluid subnode).
If you have any further questions, please don't hesitate to elaborate or share more details about what specifically does not work as expected.
Thanks for you advice!
I understood that the temperature and pressure should be uniform, but the temperature profile in the crucible is not uniform because of the heat flux on the top crucible surface. I wonder how can I make the temperature of air uniform.
I set the Enclosed Cavity as you said(Prescribed Pressure & delete Fluid node) and disabled the Boundary Load[P1(T/T1)/(1+3alpha*(T-T1))]. And I defined the Isothermal Domain for air domain for uniform temperature of air. The results seem to come out well without errors, but I would like to ask if this is the right way.
+If I disable the isothermal feature, the results come out well too. Is it okay to not apply the isothermal feature on my model?
Best,
Hyeontak Kim.
>If I understand your model correctly, I believe the Enclosed Cavity feature might still be suited for solving your problem.
>
>Note, however, that the Enclosed Cavity feature assumes that the entrapped air inside the cavity has a uniform pressure and temperature in the fluid domain, and that the gas state is governed by a global equation of state. In other words, temperature or pressure gradients cannot be resolved.
>
>Assuming that you know the air temperature (e.g. assuming thermal equilibrium between wall and gas, or solve for a heat transfer equation), you can define your equation of state for the air (e.g. ideal gas).
>
>You can then enter this equation of state either in the Fluid subnode, if you choose *User defined* from the *Compressibility* list. Alternatively, you could use the *Prescribed Pressure* subnode (and delete the *Fluid* subnode).
>
>If you have any further questions, please don't hesitate to elaborate or share more details about what specifically does not work as expected.
Thanks for you advice!
I understood that the temperature and pressure should be uniform, but the temperature profile in the crucible is not uniform because of the heat flux on the top crucible surface. I wonder how can I make the temperature of air uniform.
I set the Enclosed Cavity as you said(Prescribed Pressure & delete Fluid node) and disabled the Boundary Load[P1*(T/T1)/(1+3*alpha*(T-T1))]. And I defined the Isothermal Domain for air domain for uniform temperature of air. The results seem to come out well without errors, but I would like to ask if this is the right way.
+If I disable the isothermal feature, the results come out well too. Is it okay to not apply the isothermal feature on my model?
Best,
Hyeontak Kim.
Aaron Dettmann
COMSOL Employee
Please login with a confirmed email address before reporting spam
Posted:
9 months ago
18.07.2024, 03:14 GMT-4
I believe your approach of using the Isothermal Domain for the air temperature is good. This feature calculates a global (uniform) temperature for the air domain based on a heat transfer equation, utilizing the temperature distribution of the surrounding walls. The variable for the global temperature is named something like ht.id1.T
. This would be the temperature to use in the equation of state that you enter in the Prescribed Pressure node.
If you use only T
in the equation of state in the Prescribed Pressure node, you might end up using the boundary temperature, which is probably not what you want.
It is always beneficial to try different modeling approaches and compare the results when possible, as in this case.
I believe your approach of using the Isothermal Domain for the air temperature is good. This feature calculates a global (uniform) temperature for the air domain based on a heat transfer equation, utilizing the temperature distribution of the surrounding walls. The variable for the global temperature is named something like `ht.id1.T`. This would be the temperature to use in the equation of state that you enter in the Prescribed Pressure node.
If you use only `T` in the equation of state in the Prescribed Pressure node, you might end up using the boundary temperature, which is probably not what you want.
It is always beneficial to try different modeling approaches and compare the results when possible, as in this case.