|
[Sponsors] | |||||
|
|
|
#1 |
|
Guest
Posts: n/a
|
hi all i have simulated a rotational rheometer (Mooney viscometer) with Fluent but in the output the torque is 30% different from the sperimental data, the model for the viscosity is the non-Newtonian power law the parameter obtained from capillary rheometer. The shear rate is too high at the edge of the rotor, then the Weissenberg number is too high and i think this is the problem... what you think about? Fluent give bad data when Weissenberg number is high?
sorry for my bad english. |
|
|
||
![]() |
| Thread Tools | |
| Display Modes | |
|
|
Similar Threads
|
||||
| Thread | Thread Starter | Forum | Replies | Last Post |
| High Rayleigh Number natural convection | fly829 | FLUENT | 3 | June 7, 2011 10:41 |
| snappyHexMesh won't work - zeros everywhere! | sc298 | OpenFOAM Native Meshers: snappyHexMesh and Others | 2 | March 27, 2011 21:11 |
| air bubble is disappear increasing time using vof | xujjun | CFX | 9 | June 9, 2009 07:59 |
| Problem with Convergence at high flow rates | Syed | CD-adapco | 1 | April 10, 2007 15:18 |
| Trimmed cell and embedded refinement mesh conversion issues | michele | OpenFOAM Other Meshers: ICEM, Star, Ansys, Pointwise, GridPro, Ansa, ... | 2 | July 15, 2005 04:15 |