where τ is the shear stress, μ is the shear viscosity of the fluid, and du/dy is the derivative of the velocity component in the shear direction, relative to the perpendicular direction. Water is a good example of a Newtonian fluid. The shear viscosity of a non-Newtonian fluid is not constant, and it may even be time-dependent. The difference in mechanical properties between a Newtonian fluid and a dilitant fluid, such as Oobleck, can be seen in the figure. Oobleck can be cycled up and down the same curve; that is, the process is reversible.
Newtonian and dilitant fluids (Illustration by the author using Inkscape.) |
Compressive stress distribution in a granular medium. The compressive stress is distributed to lower particles in roughly a cone-shaped core. (Via Wikimedia Commons.) |
Discontinuous shear thickening of frictional hard-sphere suspensions at a 52% volume fraction. At low shear, there are few particles in contact (right). After a critical shear rate, there is an abrupt transition with formation of many contacting particles.(left and right images via City College of New York.)[8] |