Math 2.0

Fluid mechanics Rheology and non-Newtonian fluids Example

Power-law fluid

Example

A power-law fluid (Ostwald–de Waele fluid) has two constants, the consistency K>0K > 0 and the flow index n>0n > 0. In a simple shear flow with shear rate γ˙>0\dot\gamma > 0 its shear stress is τ=Kγ˙ n.\tau = K \dot\gamma^{\,n}. Its apparent viscosity is η(γ˙)=τ/γ˙=Kγ˙ n−1\eta(\dot\gamma) = \tau / \dot\gamma = K \dot\gamma^{\,n - 1}. For n=1n = 1 this is the constant KK, and the fluid is Newtonian. For n≠1n \ne 1 the apparent viscosity depends on γ˙\dot\gamma, so the fluid is a non-Newtonian fluid. If n<1n < 1 the viscosity decreases as γ˙\dot\gamma grows (shear-thinning, or pseudoplastic); if n>1n > 1 it increases (shear-thickening, or dilatant).

Remarks

In a general flow one writes τ=2Kγ˙ n−1D\tau = 2 K \dot\gamma^{\,n-1} D, where DD is the strain rate tensor and γ˙=2 tr⁡(D2)\dot\gamma = \sqrt{2 \, \tr(D^2)}. For n<1n < 1 the model predicts infinite viscosity at zero shear rate, so it is only used over a limited range of shear rates.

Where this leads

2 pages build on this one.

Further reading

  1. Web https://en.wikipedia.org/wiki/Power-law_fluid
About this page
TagC6RVY7R8S6
URIm2://C6RVY7R8S6
Kindexample
WritingW0 stub
MSC76A05
Instance ofNon-Newtonian fluid
Same as
Changed3 November 2026

Markdown · JSON · Edit on GitHub

What this page needs for W1

  • an inventory row: the row of the inventory that the node accounts for (0 of 1)
  • a source with a locator (0 of 1)

The writing levels say how complete the text of a page is. They do not measure its truth.

What links here

Used by