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what is a non Newtonian fluid
a fluid in which shear stress is not proportional to rate of shear
Non-Newtonian phenomena may be
time dependent
thixotropy
rheopexy
time independent
plastic flow
pseudoplastic flow
dilatant flow
plastic flow
the substance initially behaves like an elastic body and fails to flow when less amount of stress is applied. further increase in shear stress leads to increase in shear rate which progressively gets linearized.
the amount of shear stress required to break the interparticle behaves individually is called yield value.
follows Newtonian flow above yield
Dilatant
viscosity of fluid increases when shear is applied
example corn flour, wet beach sand, potassium silicate in water and starch in water
pseudoplastic
viscosity of the fluid decreases when shear is applied
eg. ketchup, polymer solution , grease
rheopectic
viscosity of the fluid increases when shear is applied
the difference from dilatant is that in rheopectic viscosity increase is time dependent
thixotropic