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Viscosity of Newtonian fluids

Gla.ss Ca.pilla.ry Viscometers. The glass capillary viscometer is widely used to measure the viscosity of Newtonian fluids. The driving force is usually the hydrostatic head of the test Hquid. Kinematic viscosity is measured directly, and most of the viscometers are limited to low viscosity fluids, ca 0.4—16,000 mm /s. However, external pressure can be appHed to many glass viscometers to increase the range of measurement and enable the study of non-Newtonian behavior. Glass capillary viscometers are low shear stress instmments 1—15 Pa or 10—150 dyn/cm if operated by gravity only. The rate of shear can be as high as 20,000 based on a 200—800 s efflux time. [Pg.180]

The viscosity of Newtonian fluids was defined as the ratio of shear stress to rate of shear r/du/dr (the conversion factor gc being temporarily... [Pg.84]

Capillary viscometers are ideal for measuring the viscosity of Newtonian fluids. However, they are unsuitable for non-Newtonian fluids since variations in hydrostatic pressure during sample efflux results in variations in shear rate and thus viscosity. This unit contains protocols for measuring the viscosity of pure liquids and solutions (see Basic Protocol) and serums from fruit juices and pastes (see Alternate Protocol). [Pg.1153]

However, they may not indicate the true bulk viscosity of a suspension that forms a thin layer of the continuous phase (e.g., serum of tomato juice) around the immersed probe or when the probe is covered by a higher viscosity gel due to fouling. Vibrational viscometers are suitable for measuring viscosities of Newtonian fluids, but not the shear-dependent rheological behavior of a non-Newtonian fluid (e.g., to calculate values of the power law parameters). [Pg.95]

Capillary viscometers have been widely used in determining the viscosity of Newtonian fluids. In these viscometers, the driving force is usually the hydrostatic head of the test liquid itself, although, application of external pressure is also used in order to increase the range of measurement and allow non-Newtonian behavior to be studied. In operation, the efflux time of a fixed volume of test liquid is measured, from which the kinematic viscosity is calculated. [Pg.281]

In this case it is no longer sufficient for one to use the constant viscosity of Newtonian fluid ( Newtonian viscosity ), r = x/y = dx/dy, as a single characteristic of the system. The so-called effective viscosity, r ef, along with the differential viscosity, dx/dy (which in this case is also the function of y), are thus introduced. At low strain rate (low shear stress) the effective viscosity is maximal. When the applied stress is increased further, the effective viscosity decreases to some minimal value and then remains unchanged with... [Pg.692]

The viscosity of Newtonian fluid is given by Margules equation ... [Pg.32]

In 1687, the empirical law of Newton related the flow stress of a fluid to its velocity gradient. The constant of proportionality was the viscosity. In fact, the viscosity describes the internal resistance of the fluid to flow and deformation. For example, water has a low resistance to flow, hence its viscosity is lower compared to most oils, for example, that have a higher resistance (at room temperature). Fluids like water and most gases are ideal fluids that satisfy Newton s theory. Many real fluids have a much more complex relationship between stress, t, and the velocity gradient, (dy/dt) (y is the deformation). The viscosity of Newtonian fluids is represented by the symbol ft whereas for real fluids, it is represented by the symbol which is also known as the dynamic viscosity ... [Pg.244]

There are several hypotheses as the rheological properties of cement pastes are concerned. As it is commonly known the rheology deals with the flowing and deformation of materials imder stress. The Newtonian fluids show a simple relationship between the shear stress and shear rate. When a thin layer of fluid is placed between the two parallel plates, of which one is fixed and the second will be subjected to the shearing force F, then the shearing of this layer will occur. The dynamic equilibrium will be attained when the force F, in the condition of stationary flow, will be balanced by the viscosity of Newtonian fluid and the relation between the shear stress and shear rate gradient will be linear (Fig. 5.1). [Pg.282]

T] = viscosity of newtonian fluid (oil) in dashpot, Pa s Total strain e = strain in the spring + strain in the dashpot... [Pg.24]

At sufficiently large strains, all solids deviate from Hooke s law. Many fluids, however, show no departures from Newtonian behavior under observable flow conditions. All gases and ordinary (nonmacromolecular) liquids are Newtonian, as are most dilute dispersions and dilute solutions of macromolecules. Viscosities of Newtonian fluids can be determined through a wide variety of methods. Many of these methods are absolute, in that the viscosity can be directly calculated from experimental measurements, without the need for calibration with a sample of known viscosity. [Pg.35]

The Influence of mo on mlnimiim film thickness is shown in Flg.k. With the increase of mo, the film will rise for same condition. The tendency is like that of Newtonian fluids reference viscosity. In fact, when power law exponent n equals one, the problem becomes Newtonian and mo equals the reference viscosity of Newtonian fluid. [Pg.234]

Here are some typical viscosities of Newtonian fluids at ambient conditions. (The viscosity of water expressed below in Ib/ft s is perhaps more familiar in Ib/ft h, that is, 6.7 x 10 x 36(X) = 2.4 Ib/ft h.)... [Pg.633]


See other pages where Viscosity of Newtonian fluids is mentioned: [Pg.180]    [Pg.689]    [Pg.560]    [Pg.46]    [Pg.367]    [Pg.22]    [Pg.560]    [Pg.82]    [Pg.51]    [Pg.558]   
See also in sourсe #XX -- [ Pg.11 , Pg.25 ]

See also in sourсe #XX -- [ Pg.497 ]




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