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Flow law

F ow Laws of Detonation. See J.F. Roth, Explosi vst 1958, 23-31 45—54, "Die ele-mentare Ableirung der StrSmungsgesetze der Detonation" (The elementary derivation of the flow laws of detonation). See also Detonation, Chapman-Jouguet Wave and Flow Behind It in Vol 4, pp D236-L to D237-L... [Pg.492]

The general features of the parabolic flow law expressed by Eq. 4.36 have been widely confirmed [12]. However, the flow process itself is more complicated than that implied above. The irregular pore space of most granular materials may better be thought of as a bundle of nonuniform capillaries, all interconnected to one another. Near the advancing solvent front the liquid is pulled into the smaller pores because of the lower rc and thus r. The large pores are left dry until more liquid arrives from the rear, at which time the cavities fill one by one from smaller to larger, but by then the semidry front has moved on. Thus the level of liquid saturation of the porous bed decreases continuously as one advances toward the front. [Pg.70]

If the flow law (strain-rate c as a function of stress a and temperature T) is known from rheological measurements, then the stress estimated from the microstructure can be used to constrain the (e, T)-regime. The strain-rate (or equivalent viscosity) can be estimated if the temperature is constrained by the mineral assemblages that are present. Conversely, the temperature can be estimated if it is assumed that e is in the range 10 -10 s . The (e, 7 )-regime may also be constrained by the Burgers vectors if the predominant slip system has been experimentally determined as a function of e and T and if these observations can be extrapolated to geological conditions. [Pg.355]

Schmid, S. M. (1982). Microfabric studies as indicators of deformation mechanisms and flow laws operative in mountain building. In Mountain Building Processes, edited by K. J. Hsii, pp. 95-110. London Academic Press. [Pg.378]

Such a wavelength will neither grow nor shrink. The fastest growing wavelength is just Aj = /3 A For a material with a non-Newtonian flow law of the form E = Epia/np), where ct and e are the equivalent stress and equivalent strain rate in tension and and Ep are material parameters, d Jo/dx is computed to be... [Pg.12]

The miCTOstructure, in particular the mean fibril spacing D, of the growing craze is a consequence of the geometry of the surface drawing process and the surface energy of the fibrils being created. It is useful to model the polymer in the active zone as a strain-softened non-Newtonian fluid with the following flow law,... [Pg.12]

Relations (9), (11) and (12) show that the associated flow law is satisfied, if Wq>0 at each moment of time. [Pg.556]

In 1955, major questions concerning the flow laws for polymer q tems still remained unanswered, however. Conclusive evidence that a is unity for short chains at constant f was lacking. The importance of polymer coil dimensions in addition to (or instead o chain length per se in the dependence of rj on molecular parameters was unknown. Similarly, the relation of Zg for different pol5miers to characteristic molecular dimensions was unknown. The usefulness of the WLF relation over a wide temperature range and the universality of the parameters in the WLF relation for a wide variety of materials 220) had not been demonstrated. [Pg.263]

With pipe diameters of this size, the molecules do not collide with each other, but solely with the walls of equipment and tubes. Therefore, different flow laws apply here than at higher pressures where the molecules collide mostly with each other. With vapours that are sensitive to heat, the collision numbers at distillation temperatures are in the hundreds of thousands. This has a negative impact on the gentle handling of the substance to be distilled. All these factors have to be taken into account for the correct evaluation of the type and size of the vacuum pumps, the tubes and the other distillation equipment. [Pg.68]

This equation is almost equivalent to the flow law derived from creep tests. A and n are the material constants, and are shown in Table 2. [Pg.652]

The effect of silica content on the flow law of the frozen sample containing Ijam silica... [Pg.655]

We found that silica particles had many effects on the mechanical behavior of ice. The most important effect was that the power law index, n, of the flow law increased with the increase of the silica contents. The relative strength changed with the silica contents and strain rates according to variations in n of the flow law. Thus, we found that the slope of the relative strength on the silica contents varied from negative to positive with the decrease of the strain rate. We also found that the sample preparation method had an important effect on the strength. The pressure-sintered sample including 1pm silica beads was always weaker than the frozen sample under the same physical conditions because the... [Pg.656]

Note that in some problems of heat and mass transfer and chemical hydrodynamics, the velocity fields near the body can be determined by the flow laws of ideal nonviscous fluid. This situation is typical of flows in a porous medium [75, 153, 346] and of interaction between bodies and liquid metals (see Section 4.11, where the solution of heat problem for a translational ideal flow past an elliptical cylinder is given). [Pg.90]

Since diffusion processes in fluids are characterized by very large values of the Schmidt number, we must point out that in problems of convective mass transfer in fluid media, the Peclet number is also large even for low Reynolds numbers at which the Stokes flow law applies (for a creeping flow). [Pg.116]

The flow law is the same for "UFg as for UFg, so no separation takes place during viscous flow. [Pg.822]

The horizontal velocity vector is found by vertical integration of the flow law (Eq. 2) ... [Pg.294]

J. Nikuradse, Stroemungsgesetze in rauhen Rohren ( Flow laws in rough tubes ), VDJ-Forsch.-Arb. Ing.-Wes. Heft 361 (1933). [Pg.544]

This paradox was resolved by Kamb (1961), who showed that it is a consequence of the hexagonal symmetry and stress dependence of flow in ice. From (8.37) or (8.46) the flow law is... [Pg.195]

The burning of waste gases through a flare stack or other device before releasing them to the air. flow law... [Pg.181]

Pressure flow is a shear flow between fixed metal boundaries, due to a pressure gradient in the melt. The pressure p falls down the streamlines, which are perpendicular to the isobars (Fig. 5.4). Appendix B derives the relationship between the pressure gradient, the channel dimensions and the flow law of the fluid. For rectangular, circular or annular cross sections, the shear stress r varies linearly across the channel, and the velocity is maximum at the centre. The Newtonian flow law in Chapter 3 is... [Pg.140]

The velocity dependence, or better the shear rate dependence, of shear stress is represented with the aid of a flow curve (shear stress x V5. shear rate T). According to Newton s definition [4], the shear rate is the velocity gradient dv/dr over the cross section of flow. The graph of the curve is described by the so called material (or flow) law or, respectively, by its coefficients. [Pg.158]

The literature [5] lists numerous different, material laws. It therefore should be noted at this point that the more coefficients a material law has, the more complicated it is to measure them, and the more difficult it is to incorporate them into equations of momentum and motion. For the calculation of an extruder, such equations yield differential-equation systems with elaborate flow laws that defy analytical resolution. Consequently, the measured flow curve should be approximated with the aid of a relatively uncomplicated material law that still adequately describes the extrusion compound. Several of the approaches used in plastics/rubber/pharma-ceutical technology include [6] power approach after Ostwald/de Waele and formulations according to Carreau, Miistedt, Casson, Herschel/ Bulk-ley, Bingham and Reiner/Philippoff... [Pg.158]

As indicated in Fig. 7, the apparent flow curve allows no geometry independent representation of the coefficients of the flow law. The yield limit, as well as the viscosity, which is determined from the slope of the curve, show different values for all three different barrel diameters. Only a geometry-independent manner of material-law representation can serve as a material-descriptive basis for calculating complicated geometries such as... [Pg.160]

GAS FLOWING LAW AROUND THE MANOMETRIC DRILL HOLE AND ITS MATHEMATICAL MODEL... [Pg.249]


See other pages where Flow law is mentioned: [Pg.213]    [Pg.617]    [Pg.629]    [Pg.362]    [Pg.3]    [Pg.3]    [Pg.25]    [Pg.52]    [Pg.3]    [Pg.4]    [Pg.555]    [Pg.294]    [Pg.653]    [Pg.655]    [Pg.655]    [Pg.656]    [Pg.656]    [Pg.294]    [Pg.296]    [Pg.637]    [Pg.140]    [Pg.161]    [Pg.930]    [Pg.1055]   
See also in sourсe #XX -- [ Pg.182 , Pg.220 ]

See also in sourсe #XX -- [ Pg.71 ]




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Basic Laws of Single-Phase Flow

Darcys Law for Viscous Flow

Darcys law through an analogy with the flow inside a network of capillary tubes

F Uniform Streaming Flow past a Solid Sphere - Stokes Law

Flow Rule and Incremental Constitutive Law

Flow of a power-law liquid between squeezing plates

Fully-developed heat transfer to power-law fluids in laminar flow

Heat transfer in laminar flow of a power-law fluid over an isothermal plane surface

Laminar and power law flows

Laminar boundary layer flow of power-law liquids over a plate

Law of resistance for single-phase flow

Laws Relate Forces to Flows

Mass transfer in laminar boundary layer flow of power- law fluids

Newton’s law of viscous flow

Poiseuille’s law for laminar flows

Second-Law Relation for Steady-State Flow Processes

The Asymptotic Laws of Freely-Ascending Convective Flows

Tube flow scaling laws

Velocity profiles in turbulent flow of power-law fluids

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