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Fluid-loaded velocity

Fig. 8.8. Analysis of line-focus-beam V(z) data for 31 different materials and orientations, compared with calculated values, (a) Normalized measured period of the oscillations in V(z) versus calculated fluid-loaded Rayleigh wave velocity the curve is eqn (8.17). (b) Normalized measured attenuation from (8.19) versus calculated attenuation the line corresponds to perfect agreement (Kushibiki and Chubachi 1985). Fig. 8.8. Analysis of line-focus-beam V(z) data for 31 different materials and orientations, compared with calculated values, (a) Normalized measured period of the oscillations in V(z) versus calculated fluid-loaded Rayleigh wave velocity the curve is eqn (8.17). (b) Normalized measured attenuation from (8.19) versus calculated attenuation the line corresponds to perfect agreement (Kushibiki and Chubachi 1985).
In the surface of a half space that is isotropic, the Rayleigh wave velocity is the same in all directions. If the surface is imagined to be in a horizontal plane, then the Rayleigh wave is composed of a shear wave component polarized in a vertical plane (SV) and a longitudinal wave component. Shear waves polarized horizontally (SH) can also exist, but they do not couple to the Rayleigh wave at all (nor, in the case of fluid loading, would they couple into waves in the fluid). [Pg.235]

Figure 3.46 Phase velocity (a) and attenuation (b) of fluid-loaded flexural plate modes plotted vs thickness/wavelength, d/A. The lossless (Scholtc) mode velocity approaches from below the velocity of the fluid, assumed to be water. CPT denotes result of classical plate theory for an unloaded plate. (Reprinted with permission. See Ref. [62].)... Figure 3.46 Phase velocity (a) and attenuation (b) of fluid-loaded flexural plate modes plotted vs thickness/wavelength, d/A. The lossless (Scholtc) mode velocity approaches from below the velocity of the fluid, assumed to be water. CPT denotes result of classical plate theory for an unloaded plate. (Reprinted with permission. See Ref. [62].)...
Changes in heat load that will affect the temperature distribution across the heat exchanger surface thereby changing the interface temperature. Fluid flow velocity. [Pg.298]

In Fig. 9.5-9 it is assumed that the temperature front (Wjj the velocity of the temperature transfer zone ) is moving with a higher speed than the ( mass transfer Zone or the breakthrough curve. In the left figure the courses of the fluid load-... [Pg.525]

Toh, M. and Murakami, Y., Velocity profiles about fluid-loaded hinged and spring-loaded scraper blades and pressure exerted on wall of an agitated vessel, Kagaku Kogaku Ronbunshu 6 417 (1980). [Pg.548]

Spring-loaded valves appear to be great strainers, especially on low ratio systems, where the fluid flow velocity is low. In this case, the valve would only crack open, presenting a very small opening through which the liquid flows, as a result, any contaminants could be trapped between the ball and seat. In some cases, crystals formed by moisture can cause valve problems. [Pg.739]

The purpose of the well completion is to provide a safe conduit for fluid flow from the reservoir to the flowline. The perforations in the casing are typically achieved by running a perforating gun into the well on electrical wireline. The gun is loaded with a charge which, when detonated, fires a high velocity jet through the casing and on into the formation for a distance of around 15-30 cm. In this way communication between the wellbore and the reservoir is established. Wells are commonly perforated after the completion has been installed and pressure tested. [Pg.227]

Decrease load to reduce wear Lower-formulation density. Decrease hed-agitation and compaction forces (e.g., mixer impeller speed, fliiid-hed height, bed weight, fluid-hed excess gas velocity, drum rotation speed). [Pg.1888]

Number of vanes. The greater the number of vanes, the lower the vane loading, and the closer the fluid follows the vanes. With higher vane loadings, the flow tends to group up on the pressure surfaces and introduces a velocity gradient at the exit. [Pg.240]

Measurements show that the velocity has a fairly constant level in the occupied zone even far downstream from the wall with the cooling device. The flow is plane, and general experience indicates that the velocity in a plane stratified flow is constant and independent of the distance from the inlet device. Prediction of the flow by coinpurational fluid dynamics shows a similar velocity level in the hall. - The full-scale measurements shown in Fig. 12.33 indicate a very low velocity in most of the hall due to the practical difficulties in obtaining a correct load during the full-scale experiment. [Pg.1187]

There are essentially three different approaches to describing hindered settling. One approach is to define a correction factor to the Stokes free settling velocity in an infinite Newtonian fluid (which we will designate F0), as a function of the solids loading. A second approach is to consider the suspending fluid properties (e.g. viscosity and density) to be modified by the... [Pg.424]


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Fluid velocity

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