Shear rate
Shear rate is the rate at which a shear is applied.
[edit] Simple Shear
The shear rate for a fluid flowing between two parallel plates, one moving at a constant speed and the other one stationary (Couette flow), is defined by

where
= The shear rate, measured in reciprocal seconds
= The velocity of the moving plate, measured in meters per second
= The distance between the two parallel plates, measured in meters
Or, 
For the simple shear case, it is just a gradient of velocity in a flowing material. The SI unit of measurement for shear rate is sec-1, expressed as "reciprocal seconds" or "inverse seconds."[1]
The shear rate at the inner wall of a Newtonian fluid flowing within a pipe[2] is:
where:
= The shear rate, measured in reciprocal seconds.
= The linear fluid velocity.
= The inside diameter of the pipe.
The linear fluid velocity v is related to the volumetric flow rate Q by:
where A is the cross-sectional area of the pipe, which for an inside pipe radius of r is given by:
thus producing:
Substituting the above into the earlier equation for the shear rate of a Newtonian fluid flowing within a pipe, and noting (in the denominator) that d = 2r:
which simplifies to the following equivalent form for wall shear rate in terms of volumetric flow rate Q and inner pipe radius r :
For a Newtonian fluid wall shear stress (τw) can be related to shear rate by
, where μ is the viscosity of the fluid. For Non-Newtonian fluids, there are different constitutive laws depending on the fluid, which relates the stress tensor to the shear rate tensor.
[edit] References
- ^ "Brookfield Engineering - Glossary section on Viscosity Terms". http://www.brookfieldengineering.com/education/viscosity_glossary.asp. Retrieved 2007-06-10.
- ^ Ron Darby, Chemical engineering fluid mechanics, 2nd ed. CRC Press, 2001, p. 64
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= The shear rate, measured in reciprocal seconds
= The velocity of the moving plate, measured in meters per second
= The distance between the two parallel plates, measured in meters
= The inside diameter of the pipe.



