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                                                Posted:
                            
                                1 decade ago                            
                            
                                26 apr 2011, 10:49 GMT-4                            
                        
                        
                                                    In the initial conditions, give the model as starting point the velocity that you used at your inlet. 
That might remove your warning message,
Luis                                                
                                                
                            In the initial conditions, give the model as starting point the velocity that you used at your inlet. 
That might remove your warning message,
Luis                        
                                                
                                                                                                            
                                             
                                            
                            
                                                                                        
                                Ivar KJELBERG
                                                                                                                                                    COMSOL Multiphysics(r) fan, retired, former "Senior Expert" at CSEM SA (CH)
                                                         
                            
                         
                                                
    
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                                                Posted:
                            
                                1 decade ago                            
                            
                                26 apr 2011, 15:06 GMT-4                            
                        
                        
                                                    Hi
My advice is also going in that direction, I have noticed, that helping the solver with some "good" initial condition guesses, improves a lot the time to results. In fact for simple fluid flow cases, I mostly apply a parabolic velocity profile, as initial and inlet conditions, and for the initial pressure drop I use Poiseuille law to have a pressure gradient along the flow line. 
Then too check the Reynolds cell number to be sure you are in laminar flow conditions, when you apply it, this might give an indication about the mesh size ratio.
Finally use "boundary mesh layers along the non-slip walls, this is not yet always implemented in the "default physics settings of COMSOL mesher
--
Good luck
Ivar                                                
                                                
                            Hi
My advice is also going in that direction, I have noticed, that helping the solver with some "good" initial condition guesses, improves a lot the time to results. In fact for simple fluid flow cases, I mostly apply a parabolic velocity profile, as initial and inlet conditions, and for the initial pressure drop I use Poiseuille law to have a pressure gradient along the flow line. 
Then too check the Reynolds cell number to be sure you are in laminar flow conditions, when you apply it, this might give an indication about the mesh size ratio.
Finally use "boundary mesh layers along the non-slip walls, this is not yet always implemented in the "default physics settings of COMSOL mesher
--
Good luck
Ivar                        
                                                
                                                                                                            
                                             
                                            
                                                
    
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                                                Posted:
                            
                                1 decade ago                            
                            
                                26 apr 2011, 15:26 GMT-4                            
                        
                        
                                                    Hi Ivar,
Could you please guide me how to calculate pressure drop for the flow between two parallel plates (square duct). I think Poiseuille law is for the circular pipe flow..
thanks
Mayur                                                 
                                                
                            Hi Ivar,
Could you please guide me how to calculate pressure drop for the flow between two parallel plates (square duct). I think Poiseuille law is for the circular pipe flow..
thanks
Mayur                         
                                                
                                                                                                            
                                             
                        
                        
                            
                                                                                        
                                Ivar KJELBERG
                                                                                                                                                    COMSOL Multiphysics(r) fan, retired, former "Senior Expert" at CSEM SA (CH)
                                                         
                            
                         
                                                
    
        Please login with a confirmed email address before reporting spam
     
    
 
                                                Posted:
                            
                                1 decade ago                            
                            
                                26 apr 2011, 16:15 GMT-4                            
                        
                        
                                                    Hi
you are right for Poiseuille, I overlooked your 2D parallel plate comment, went back to my pipe issue ;)
My main comment was if you have difficulties to get the solver to converge, any good estimates is better than a flat "0". You need some pressure build-up to drive a flow, then you must use your common physics sense, and perhaps iterate, or repeat the solver sequence with something close to the first solution found (used as initial conditions for second attempt) just to check that the solution remains the same
--
Good luck
Ivar                                                
                                                
                            Hi
you are right for Poiseuille, I overlooked your 2D parallel plate comment, went back to my pipe issue ;)
My main comment was if you have difficulties to get the solver to converge, any good estimates is better than a flat "0". You need some pressure build-up to drive a flow, then you must use your common physics sense, and perhaps iterate, or repeat the solver sequence with something close to the first solution found (used as initial conditions for second attempt) just to check that the solution remains the same
--
Good luck
Ivar