Stress tensor for non-Newtonian fluid

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Setting up the stress tensor for a non-Newtonian fluid involves using the same equations as for Newtonian fluids, with viscosity represented as a function of the second invariant of the rate of deformation tensor. For power law fluids, the shear stress in the flow direction is expressed as K(du/dy)^n, indicating that the normal stresses are pressure-related. In symmetric pipe or rectangular duct scenarios, it is suggested that other stress components may be zero. The discussion emphasizes the importance of understanding the relationship between shear stress and deformation in non-Newtonian fluids. Properly defining the stress tensor is crucial for accurate modeling of fluid behavior in various applications.
ccrook
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How does one setup the stress tensor for a non-Newtonian fluid? I know that for any fluid the normals should be the pressure and for a power law fluid the shear stress in the direction of flow is related by K(du/dy)^n. Does this mean that all other components are 0 for a symmetric pipe or rectangular duct?
 
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ccrook said:
How does one setup the stress tensor for a non-Newtonian fluid? I know that for any fluid the normals should be the pressure and for a power law fluid the shear stress in the direction of flow is related by K(du/dy)^n. Does this mean that all other components are 0 for a symmetric pipe or rectangular duct?
For a purely viscous non-Newtonian fluid (not viscoelastic), you use exactly the same form of equation as for a Newtonian fluid (see Bird, Stewart, and Lightfoot), except that you represent the viscosity as a function of the 2nd invariant of the rate of deformation tensor. There is a form of this functionality that gives the same behavior as a power law fluid for simple shear flows.

Chet
 
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