Hello Dieng Abdoulaye
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Posted:
9 years ago
2016年1月20日 GMT-5 01:29
Hi,i want to know whether you have solved the problem . Now i face with the same question . thank you best wishes to you
Hi,i want to know whether you have solved the problem . Now i face with the same question . thank you best wishes to you
Jeff Hiller
COMSOL Employee
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Posted:
9 years ago
2016年1月20日 GMT-5 08:36
A simple model that may interest you is here:
www.comsol.com/model/separation-through-dialysis-258
In that model, the velocity in the free flow regions can be assumed, so we're only solving for the concentrations.
If you wish to solve for the velocities (which seems to be the case, judging from your post), a more sophisticated approach involving the coupling of free and porous medium flow is illustrated by this model:
www.comsol.com/model/porous-reactor-with-injection-needle-25
There are several other tutorials that show how to couple free and porous medium flow in the Application Libraries for the Chemical Reaction Engineering Module (see
www.comsol.com/chemical-reaction-engineering-module) and the Subsurface Flow Module (see
www.comsol.com/subsurface-flow-module) if you have them on your license.
Best regards,
Jeff
A simple model that may interest you is here:
http://www.comsol.com/model/separation-through-dialysis-258
In that model, the velocity in the free flow regions can be assumed, so we're only solving for the concentrations.
If you wish to solve for the velocities (which seems to be the case, judging from your post), a more sophisticated approach involving the coupling of free and porous medium flow is illustrated by this model:
http://www.comsol.com/model/porous-reactor-with-injection-needle-25
There are several other tutorials that show how to couple free and porous medium flow in the Application Libraries for the Chemical Reaction Engineering Module (see http://www.comsol.com/chemical-reaction-engineering-module) and the Subsurface Flow Module (see http://www.comsol.com/subsurface-flow-module) if you have them on your license.
Best regards,
Jeff
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Posted:
9 years ago
2016年5月24日 GMT-4 15:27
the examples i looked but i don´t get permeation of hidrogeno.(2D)
I put a domain where the fluid goes in direction axial but the right domain is a porous membrane so the fluid to have goes also in direcction radial and third domain is permeation and goes in direcction velocity axial.
My example is similary a dialysis but my driving force is the pressure and i don´t get across the membrane .
the examples i looked but i don´t get permeation of hidrogeno.(2D)
I put a domain where the fluid goes in direction axial but the right domain is a porous membrane so the fluid to have goes also in direcction radial and third domain is permeation and goes in direcction velocity axial.
My example is similary a dialysis but my driving force is the pressure and i don´t get across the membrane .