Lars Dammann
COMSOL Employee
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Posted:
5 years ago
24 févr. 2020, 03:20 UTC−5
Hi Bilal, you can specify boundary conditions that depend on time, for example you can define T to be 20[degC]+t*1[K/s]
to start with 20° at t=0 and then increase the temperature over time. You can also define helper functions to make this easier. Please note that your boundary conditions should be continuous in time. If you have sudden jumps, you may want to use the events interface. This blog shows an example of that: https://www.comsol.de/blogs/implementing-a-thermostat-with-the-events-interface/
Best wishes,
Lars
Hi Bilal, you can specify boundary conditions that depend on time, for example you can define T to be `20[degC]+t*1[K/s]` to start with 20° at t=0 and then increase the temperature over time. You can also define helper functions to make this easier. Please note that your boundary conditions should be continuous in time. If you have sudden jumps, you may want to use the events interface. This blog shows an example of that: https://www.comsol.de/blogs/implementing-a-thermostat-with-the-events-interface/
Best wishes,
Lars
Lars Gregersen
COMSOL Employee
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Posted:
5 years ago
24 févr. 2020, 04:24 UTC−5
This model
https://www.comsol.com/model/convective-heat-transfer-with-pseudo-periodicity-12057
Should give you an idea of how to do what you describe.
-------------------
Lars Gregersen
Comsol Denmark
This model
https://www.comsol.com/model/convective-heat-transfer-with-pseudo-periodicity-12057
Should give you an idea of how to do what you describe.
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Posted:
5 years ago
24 févr. 2020, 11:06 UTC−5
Thanks for your help. I learned new things from them but these two examples were dealing with different scenarios of mine:
1. for the thermostat there is an on/off point scenario
2. and the convective heat transfer with phseudo periodicty is related to different sections (I used this model before for two pipe in which I could
, but for me it is not the boundry condition. it is various inlet temperatures (for a pipe) but the problem is the outlet temperature (heat outflow) of first step is going to be the inlet temperature for the second step.
I really appreciate your help.
Thanks for your help. I learned new things from them but these two examples were dealing with different scenarios of mine:
1. for the thermostat there is an on/off point scenario
2. and the convective heat transfer with phseudo periodicty is related to different sections (I used this model before for two pipe in which I could
, but for me it is not the boundry condition. it is various inlet temperatures (for a pipe) but the problem is the outlet temperature (heat outflow) of first step is going to be the inlet temperature for the second step.
I really appreciate your help.