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Dean Flow Modelling in MicroChannels
Posted Sep 24, 2015, 6:15 a.m. EDT MEMS & Nanotechnology, MEMS & Piezoelectric Devices, Microfluidics, Structural Mechanics Version 5.0 3 Replies
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Hi,
I'm trying to model Dean Flow in a Spiral Microchannel for further application of Passive Cell Separation.
Since Dean Flow is observed basically on the plane which is perpendicular to the downstream fluid flow, it requires 3D modelling of channel geometry. ( Here there is a schematic explanation: pubs.rsc.org/services/images/RSCpubs.ePlatform.Service.FreeContent.ImageService.svc/ImageService/Articleimage/2010/CS/b915999c/b915999c-f17.gif )
I modelled the spiral geometry, defined the material as water, did 'finer' mesh, specified the inlet and outlet, and their corresponding boundary conditions as velocity, where the outlet velocity is half of the inlet velocity since there is one inlet and two outlets with same cros-sectional areas.
I did all of this in Creeping Flow module... Actually this might be problematic since the Reynold's number in the system is 1.27 ( channel cros-section : 130x500 um , and inlet velocity : 7.6 mm/s )
When I tried solve it for Stationary Flow, I couldn't get a convergence after waiting 36 hours ( Here is a screenshoot that i took just befor cancelling the computation : postimg.org/image/48uqj45wn/ )
Are there anyone who have modelled Dean Flow before?
At what point I'm making a wrong thing?
Any advice or suggestion will be appreciated :)
Thanks in advance
I'm trying to model Dean Flow in a Spiral Microchannel for further application of Passive Cell Separation.
Since Dean Flow is observed basically on the plane which is perpendicular to the downstream fluid flow, it requires 3D modelling of channel geometry. ( Here there is a schematic explanation: pubs.rsc.org/services/images/RSCpubs.ePlatform.Service.FreeContent.ImageService.svc/ImageService/Articleimage/2010/CS/b915999c/b915999c-f17.gif )
I modelled the spiral geometry, defined the material as water, did 'finer' mesh, specified the inlet and outlet, and their corresponding boundary conditions as velocity, where the outlet velocity is half of the inlet velocity since there is one inlet and two outlets with same cros-sectional areas.
I did all of this in Creeping Flow module... Actually this might be problematic since the Reynold's number in the system is 1.27 ( channel cros-section : 130x500 um , and inlet velocity : 7.6 mm/s )
When I tried solve it for Stationary Flow, I couldn't get a convergence after waiting 36 hours ( Here is a screenshoot that i took just befor cancelling the computation : postimg.org/image/48uqj45wn/ )
Are there anyone who have modelled Dean Flow before?
At what point I'm making a wrong thing?
Any advice or suggestion will be appreciated :)
Thanks in advance
3 Replies Last Post Oct 6, 2015, 5:47 a.m. EDT