Rheological Deformation Properties of AB Materials A

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FINAL EXAMINATION 32949427

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Grace Balahay

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Rheological Deformation Properties of AB Materials A


Rheological Deformation Properties of AB Materials AVersión en línea FINAL EXAMINATION 32949427 por Grace Balahay 1 has been used to interpret stress relaxation of viscoelastic liquids, especially polymeric liquid a Maxwell Model b Kelvin-Voigt Model c Burger Model 2 Creep behavior can be described. This model contains a spring and a dashpot connected in parallel a Kelvin-Voigt Model b Maxwell Model c Burger Model 3 proposed, which is the series combination of the Kelvin and Maxwell a Burger Model b Kelvin-Voigt Model c Maxwell Model 4 follows the Bingham curve characterized by straight line with y-intercept above the origin a flow behavior of plastic materials b flow behavior of viscous materials 5 follows either with the Newtonian curve, which is a straight line originating from the origin, or the non-newtonian curve. a flow behavior of plastic materials b flow behavior of viscous materials 6 is defined to make the transport properties analogous. Its unit is m 2 /s in SI and stoke (cm2 /s) in CGS. It is the ratio of dynamic viscosity to density of fluid: a Momentum diffusivity or kinematic viscosity b Newtonian Fluids c d 7 tend to deform continuously under the effect of an applied stress. a Viscous Fluids b Non-Newtonian Fluids c Newtonian Fluids 8 The ratio of shear stress to the corresponding shear rate is therefore a apparent viscosity b Newtonian viscosity c Non-Newtonian Fluids 9 In these types of fluids, as shear rate increases friction between layers decreases. a Shear Thinning (Pseudoplastic) Fluids b Shear Thickening Fluids 10 In these types of fluids, as shear rate increases, the internal friction and apparent viscosity increase. a Shear Thickening Fluids b Shear Thinning (Pseudoplastic) Fluids 11 In these types of fluids, fluid remains rigid when the magnitude of shear stress is smaller than the yield stress but flows like a Newtonian fluid when the shear stress exceeds . a Bingham Plastic Fluids b Non-Bingham Plastic Fluids c d 12 In these types of fluids, a minimum shear stress known as yield stress must be exceeded before flow begins, a Non-Bingham Plastic Fluids b Non-Bingham Plastic Fluids c d 13 are those that exhibit decreasing shear stress and apparent viscosity with respect to time at a fixed shear rate (shear thinning with time). This phenomenon is probably due to the breakdown in the structure of the material as shearing continues. Gelatin, egg white, and shortening can be given as examples of this type of fluid. a Thixotropic fluids b Thixotropic behavior c rheopectic fluids d 14 may be reversible, partially reversible, or irreversible when the applied shear is removed (fluid is allowed to be at rest). Irreversible thixotropy is called rheomalaxis or rheodestruction. a Thixotropic behavior b Thixotropic fluids c rheopectic fluids d 15 (shear thickening with time), shear stress and apparent viscosity increase with time, that is, the structure builds up as shearing continues (Fig. 6). Bentonite clay suspensions show this type of flow behavior. It is rarely observed in food systems. a rheopectic fluids b Thixotropic fluids c Thixotropic behavior d 16 are generally in the form of a U-tube. These types of viscometers are very simple, inexpensive, and suitable for low-viscosity fluids. a Capillary Flow Viscometers b Rotational Viscometers c Falling Ball Viscometers d Orifice Type Viscometers 17 the time for a standard volume of fluid to flow through an orifice is measured. They are used for Newtonian or near-Newtonian fluids when extreme accuracy is not required. a Orifice Type Viscometers b Capillary Flow Viscometers c Falling Ball Viscometers d Rotational Viscometers 18 These types of viscometers involve a vertical tube where a ball is allowed to fall under the influence of gravity. It operates on the principle of measuring the time for a ball to fall through a liquid under the influence of gravity a Falling Ball Viscometers b Rotational Viscometers c Orifice Type Viscometers d 19 the sample is sheared between the two parts of the measuring device by means of rotation. In agitation, the shear rate is proportional to the rotational speed. a Rotational Viscometers b Orifice Type Viscometers c Orifice Type Viscometers d

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Rheological Deformation Properties of AB Materials AVersión en línea

por Grace Balahay

has been used to interpret stress relaxation of viscoelastic liquids, especially polymeric liquid

Creep behavior can be described. This model contains a spring and a dashpot connected in parallel

proposed, which is the series combination of the Kelvin and Maxwell

follows the Bingham curve characterized by straight line with y-intercept above the origin

follows either with the Newtonian curve, which is a straight line originating from the origin, or the non-newtonian curve.

is defined to make the transport properties analogous. Its unit is m 2 /s in SI and stoke (cm2 /s) in CGS. It is the ratio of dynamic viscosity to density of fluid:

tend to deform continuously under the effect of an applied stress.

The ratio of shear stress to the corresponding shear rate is therefore

In these types of fluids, as shear rate increases friction between layers decreases.

In these types of fluids, as shear rate increases, the internal friction and apparent viscosity increase.

In these types of fluids, fluid remains rigid when the magnitude of shear stress is smaller than the yield stress but flows like a Newtonian fluid when the shear stress exceeds .

In these types of fluids, a minimum shear stress known as yield stress must be exceeded before flow begins,

may be reversible, partially reversible, or irreversible when the applied shear is removed (fluid is allowed to be at rest). Irreversible thixotropy is called rheomalaxis or rheodestruction.

(shear thickening with time), shear stress and apparent viscosity increase with time, that is, the structure builds up as shearing continues (Fig. 6). Bentonite clay suspensions show this type of flow behavior. It is rarely observed in food systems.

are generally in the form of a U-tube. These types of viscometers are very simple, inexpensive, and suitable for low-viscosity fluids.

the time for a standard volume of fluid to flow through an orifice is measured. They are used for Newtonian or near-Newtonian fluids when extreme accuracy is not required.

These types of viscometers involve a vertical tube where a ball is allowed to fall under the influence of gravity. It operates on the principle of measuring the time for a ball to fall through a liquid under the influence of gravity

the sample is sheared between the two parts of the measuring device by means of rotation. In agitation, the shear rate is proportional to the rotational speed.