Disambiguation evidence for Newtonian fluids via surface form
"Newtonian fluid"
As subject (48)
Triples where this entity appears as subject under the
label "Newtonian fluid".
| Predicate | Object |
|---|---|
| appliesTo | simple shear flows ⓘ |
| appliesTo | unidirectional laminar flow ⓘ |
| assumptionIn | derivation of Navier–Stokes equations ⓘ |
| contrastedWith | non-Newtonian fluid ⓘ |
| dependsOn | pressure for viscosity value ⓘ |
| dependsOn | temperature for viscosity value ⓘ |
| describedBy |
Newtonian fluids
self-linksurface differs
ⓘ
surface form:
Newton’s law of viscosity
|
| hasExample | air at standard conditions ⓘ |
| hasExample | light mineral oils ⓘ |
| hasExample | most simple gases ⓘ |
| hasExample | water at moderate conditions ⓘ |
| hasLimitation | does not capture viscoelastic effects ⓘ |
| hasLimitation | does not model polymer melts accurately ⓘ |
| hasLimitation | does not model suspensions accurately ⓘ |
| hasParameter | dynamic viscosity μ ⓘ |
| hasParameter | kinematic viscosity ν ⓘ |
| hasProperty | constant viscosity at given temperature and pressure ⓘ |
| hasProperty | isotropic viscous behavior ⓘ |
| hasProperty | linear constitutive relation between stress and rate-of-strain tensor ⓘ |
| hasProperty | linear stress–strain-rate relationship ⓘ |
| hasProperty | no normal stress differences in simple shear ⓘ |
| hasProperty | no shear-thickening behavior ⓘ |
| hasProperty | no shear-thinning behavior ⓘ |
| hasProperty | no viscoelastic memory effects ⓘ |
| hasProperty | no yield stress ⓘ |
| hasProperty | normal stresses proportional to volumetric strain rate ⓘ |
| hasProperty | rate-type behavior without elasticity ⓘ |
| hasProperty | shear stress proportional to shear rate ⓘ |
| hasProperty | stress depends only on instantaneous rate of deformation ⓘ |
| hasProperty | time-independent viscosity ⓘ |
| hasProperty | viscosity independent of flow history ⓘ |
| hasProperty | viscosity independent of shear rate ⓘ |
| instanceOf | continuum material ⓘ |
| instanceOf | fluid ⓘ |
| instanceOf | idealized fluid model ⓘ |
| mathematicalForm | τ_ij = 2 μ e_ij + λ δ_ij ∇·v ⓘ |
| namedAfter | Isaac Newton ⓘ |
| obeysEquation | τ = μ (du/dy) ⓘ |
| usedAs | baseline assumption in many engineering calculations ⓘ |
| usedAs | reference model in rheology ⓘ |
| usedIn | Navier–Stokes equations ⓘ |
| usedIn | boundary layer theory ⓘ |
| usedIn | computational fluid dynamics ⓘ |
| usedIn | continuum mechanics ⓘ |
| usedIn | fluid mechanics ⓘ |
| usedIn | lubrication theory ⓘ |
| usedIn | pipe flow analysis ⓘ |
| usedIn | rheology ⓘ |