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Viscosity transverse

The transverse viscosity //. is negligibly small in the wave propagation ... [Pg.73]

Fig. 6 The effect of transverse viscosity on the polar plot of Fig. 4. The damping coefficient, a, is plotted vs. the real capillary wave frequency, 0> for several different transverse viscosities (/x in the figure has units of 10 5 mNsm ). Only the isopleths for Sd = 0 and k = 0 are shown to give the outermost loop of Fig. 4. The plot was generated using the same condition as in Fig. 4, k = 32 431 m, ad = 71.97mN nr1, p = 997.0 kg nr3, r) = 0.894 mPa s and g = 9.80 m s 2... Fig. 6 The effect of transverse viscosity on the polar plot of Fig. 4. The damping coefficient, a, is plotted vs. the real capillary wave frequency, 0> for several different transverse viscosities (/x in the figure has units of 10 5 mNsm ). Only the isopleths for Sd = 0 and k = 0 are shown to give the outermost loop of Fig. 4. The plot was generated using the same condition as in Fig. 4, k = 32 431 m, ad = 71.97mN nr1, p = 997.0 kg nr3, r) = 0.894 mPa s and g = 9.80 m s 2...
If we choose the coefficients p and s in (6.1.7) to be nonzero constants, then we arrive at the Reiner-Rivlin model, which additively combines the Newton model with a tensor-quadratic component. In this case the constants p and e are called, respectively, the shear and the dilatational (transverse) viscosity. Equation (6.1.7) permits one to give a qualitative description of specific features of the mechanical behavior of viscoelastic fluids, in particular, the Weissenberg effect (a fluid rises along a rotating shaft instead of flowing away under the action of the centrifugal force). [Pg.264]

Let the relative viscosity (normalized by the suspending fluid viscosity) as measured in the direction of the cylinder axis (longitudinal direction) as prL and the relative transverse viscosity be / rT. At the low shear limit and in a dilute system, the viscosity is expected to be isotropic. Eshelby (100) obtained... [Pg.140]

Equation 50 does not agree with the experimentally observed Quemada equation. However, by comparing equations 48 and 49 with 50, we may expect that the longitudinal viscosity of the cylindrical fiber suspension is smaller than the viscosity of spherical particle suspensions at a concentrated state, whereas the transverse viscosity is higher than the viscosity of spherical suspensions. [Pg.141]

Pokrovskii [112] demonstrated theoretically that concentrated suspensions of solid ellipsoidal bodies in a Newtonian fluid give rise to a viscoelastic behavior. He showed that for such suspensions it is possible to use the concept of transverse viscosity which expresses the effect of normal stresses and found that the transverse viscosity increases with velocity gradient. [Pg.86]

The issues of the proper radial boundary condition for the pressure and the effect of a transverse viscosity gradient are treated in... [Pg.82]

The approach used by Tadmor and Gogos, which is the conventional one in the literature, leads to a radial stress that is independent of z and will give the incorrect force for a fluid with a transverse viscosity gradient (which would be expected for a power-law fluid at high... [Pg.82]

Multidimensionality may also manifest itself in the rate coefficient as a consequence of anisotropy of the friction coefficient [M]- Weak friction transverse to the minimum energy reaction path causes a significant reduction of the effective friction and leads to a much weaker dependence of the rate constant on solvent viscosity. These conclusions based on two-dimensional models also have been shown to hold for the general multidimensional case [M, 59, and 61]. [Pg.851]

In these equations x and y denote independent spatial coordinates T, the temperature Tib, the mass fraction of the species p, the pressure u and v the tangential and the transverse components of the velocity, respectively p, the mass density Wk, the molecular weight of the species W, the mean molecular weight of the mixture R, the universal gas constant A, the thermal conductivity of the mixture Cp, the constant pressure heat capacity of the mixture Cp, the constant pressure heat capacity of the species Wk, the molar rate of production of the k species per unit volume hk, the speciflc enthalpy of the species p the viscosity of the mixture and the diffusion velocity of the A species in the y direction. The free stream tangential and transverse velocities at the edge of the boundaiy layer are given by = ax and Vg = —ay, respectively, where a is the strain rate. The strain rate is a measure of the stretch in the flame due to the imposed flow. The form of the chemical production rates and the diffusion velocities can be found in (7-8). [Pg.406]

To model this, Duncan-Hewitt and Thompson [50] developed a four-layer model for a transverse-shear mode acoustic wave sensor with one face immersed in a liquid, comprised of a solid substrate (quartz/electrode) layer, an ordered surface-adjacent layer, a thin transition layer, and the bulk liquid layer. The ordered surface-adjacent layer was assumed to be more structured than the bulk, with a greater density and viscosity. For the transition layer, based on an expansion of the analysis of Tolstoi [3] and then Blake [12], the authors developed a model based on the nucleation of vacancies in the layer caused by shear stress in the liquid. The aim of this work was to explore the concept of graded surface and liquid properties, as well as their effect on observable boundary conditions. They calculated the hrst-order rate of deformation, as the product of the rate constant of densities and the concentration of vacancies in the liquid. [Pg.76]

In Eq. (1) Riu) is the longitudinal i = 1) or transverse i = 2) relaxation rate of the bulk water protons, corresponding to that measured for an analogous diamagnetic solution. In practice, Ri, coincides with the value determined for pure water under identical conditions of pH, temperature, and observation frequency. Clearly, the above relation strictly holds only for dilute solutions, in the absence of solute-solute interactions and of variations in viscosity. [Pg.177]

In FFF, separation is determined by the combined action of the nonuniform flow profile and transverse field effects. The classical configuration assumes the FFF channel as two infinite parallel plates (see Figure 12.4), of which the accumulation wall lies at x=0, where x is the cross-channel axis (directed upward from the accumulation wall). Inside the channel, the carrier fluid, assumed to have a constant viscosity, has a velocity profile u(x) that takes the form... [Pg.331]

Burton has likewise investigated the effect of the medium on the mobility and on the transverse potential fall since these should be dependent both on the viscosity and oh the specific inductive capacity as typical of the results obtained the following may be cited ... [Pg.231]


See other pages where Viscosity transverse is mentioned: [Pg.68]    [Pg.92]    [Pg.141]    [Pg.176]    [Pg.352]    [Pg.368]    [Pg.778]    [Pg.778]    [Pg.68]    [Pg.92]    [Pg.141]    [Pg.176]    [Pg.352]    [Pg.368]    [Pg.778]    [Pg.778]    [Pg.379]    [Pg.664]    [Pg.585]    [Pg.557]    [Pg.344]    [Pg.540]    [Pg.120]    [Pg.66]    [Pg.293]    [Pg.657]    [Pg.213]    [Pg.241]    [Pg.104]    [Pg.151]    [Pg.87]    [Pg.137]    [Pg.11]    [Pg.265]    [Pg.92]    [Pg.223]    [Pg.255]    [Pg.166]    [Pg.395]    [Pg.181]    [Pg.36]    [Pg.179]    [Pg.213]    [Pg.333]   
See also in sourсe #XX -- [ Pg.264 ]




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Transverse pressure, flow/viscosity

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