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Rheology usefulness

The Crossian rheology, when compared to the Newtonian rheology using the low shear viscosity, has a laiger thickness and the same dependence on substrate velocity (Le., /U. To date, this theoiy... [Pg.641]

Rheological measurements on the slurry have been performed by Bohlin rheometer model VOR and constant stress rheometer C.. These two units combined are powerful enough to analyze slurries completely in viscometry, oscillatory and relaxation tests. Injection molding compound is fully characterized rheologically using capillary rheometer. [Pg.37]

Function in Formula To provide vi.scosity, stabilization, and rheology Use Concentration 0.1-1% in water-based gels 0.1-0.3% in emulsions Solubility Characteristics Soluble in w ater... [Pg.626]

Table 1 Fractal Dimension Calculated Via Image Analysis Compared to Fractal Dimension Calculated Via Rheology Using the Weak-Link Theory ... [Pg.85]

For step strain or steady flow, the deformation in the bulk may still be uniform, and if the true strain or strain rate is known, useful data can be obtained by correcting the data for slip. But in transient flows, the slip transient is superposed on the viscoelastic response, and rheologically useful information cannot normally be obtained. [Pg.371]

A third definition of surface mobility is essentially a rheological one it represents the extension to films of the criteria we use for bulk phases and, of course, it is the basis for distinguishing states of films on liquid substrates. Thus as discussed in Chapter IV, solid films should be ordered and should show elastic and yield point behavior liquid films should be coherent and show viscous flow gaseous films should be in rapid equilibrium with all parts of the surface. [Pg.711]

Neither the thermodynamic nor the rheological description of surface mobility has been very useful in the case of chemisorbed films. From the experimental point of view, the first is complicated by the many factors that can affect adsorption entropies and the latter by the lack of any methodology. [Pg.711]

Tanner, R.I. 2000. Engineering Rheology, 2nd edti, Oxford University Press, Oxford. Taylor, C., Ranee, J. and Medwell, J. O., 1985. A note on the imposition of traction boundary conditions when using FEM for solving incompressible flow problems. Comnmn. Appl. Numer. Methods 1, 113-121. [Pg.110]

Incorporation of viscosity variations in non-elastic generalized Newtonian flow models is based on using empirical rheological relationships such as the power law or Carreau equation, described in Chapter 1. In these relationships fluid viscosity is given as a function of shear rate and material parameters. Therefore in the application of finite element schemes to non-Newtonian flow, shear rate at the elemental level should be calculated and used to update the fluid viscosity. The shear rale is defined as the second invariant of the rate of deformation tensor as (Bird et at.., 1977)... [Pg.126]

Step 4 - update the value of viscosity (r/) using an appropriate rheological equation (e.g. temperature-dependent form of the Carreau model given as Equation (5.4)). [Pg.169]

GETMAT Reads and echo prints physical and rheological parameters and the penalty parameter used in the simulation. [Pg.213]

Note that convected derivatives of the stress (and rate of strain) tensors appearing in the rheological relationships derived for non-Newtonian fluids will have different forms depending on whether covariant or contravariant components of these tensors are used. For example, the convected time derivatives of covariant and contravariant stress tensors are expressed as... [Pg.263]

Fats contribute to the rheological properties in flowable and pastry foods. By combining with starches to form a clathrate, a product different from the native starch is formed, eg, shortening in baked goods. The highly developed shortness of pies baked in eadier times resulted from the use of high levels of lard. The use of less fat in pie cmsts is evident, ie, the cmsts are harder and readily become soggy. [Pg.117]

LOY is characterized by low spinning tension, mostiy rheological effects, Httie orientation, amorphous stmcture, low tensde strength, and high elongation. The spun filament must be drawn, usually three to six times its initial length, and heat-treated before it develops useful properties. Nearly all PET staple is spun this way. [Pg.330]

One simple rheological model that is often used to describe the behavior of foams is that of a Bingham plastic. This appHes for flows over length scales sufficiently large that the foam can be reasonably considered as a continuous medium. The Bingham plastic model combines the properties of a yield stress like that of a soHd with the viscous flow of a Hquid. In simple Newtonian fluids, the shear stress T is proportional to the strain rate y, with the constant of proportionaHty being the fluid viscosity. In Bingham plastics, by contrast, the relation between stress and strain rate is r = where is... [Pg.430]

Foams have a wide variety of appHcations that exploit their different physical properties. The low density, or high volume fraction of gas, enable foams to float on top of other fluids and to fiU large volumes with relatively Httle fluid material. These features are of particular importance in their use for fire fighting. The very high internal surface area of foams makes them useful in many separation processes. The unique rheology of foams also results in a wide variety of uses, as a foam can behave as a soHd, while stiH being able to flow once its yield stress is exceeded. [Pg.431]

Solutions of rhamsan have high viscosity at low shear rates and low gum concentrations (90). The rheological properties and suspension capabiUty combined with excellent salt compatibihty, make it useful for several industrial apphcations including agricultural fertilizer suspensions, pigment suspensions, cleaners, and paints and coatings. [Pg.437]


See other pages where Rheology usefulness is mentioned: [Pg.169]    [Pg.94]    [Pg.369]    [Pg.148]    [Pg.765]    [Pg.165]    [Pg.61]    [Pg.66]    [Pg.616]    [Pg.2301]    [Pg.128]    [Pg.43]    [Pg.72]    [Pg.111]    [Pg.169]    [Pg.94]    [Pg.369]    [Pg.148]    [Pg.765]    [Pg.165]    [Pg.61]    [Pg.66]    [Pg.616]    [Pg.2301]    [Pg.128]    [Pg.43]    [Pg.72]    [Pg.111]    [Pg.193]    [Pg.545]    [Pg.562]    [Pg.80]    [Pg.143]    [Pg.230]    [Pg.322]    [Pg.48]    [Pg.49]    [Pg.315]    [Pg.367]    [Pg.367]    [Pg.426]    [Pg.432]    [Pg.432]    [Pg.291]    [Pg.297]    [Pg.453]   
See also in sourсe #XX -- [ Pg.39 , Pg.62 ]




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Blend Rheology Using the Palieme Model

Dimensionless Groups Used to Plot Rheological Data

Rheology methods used

Treatment of Rheological Data Using Models

Use as rheological additives

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