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Viscosity gradient

The effects of flow nonuniformities, in particular, can be severe in gas systems when the ratio of bed-to-particle diameters is small in liquid systems when viscous fingering occurs as a result of large viscosity gradients in the adsorption bed when very small particles (<50 Im) are used, such as in high performance liqmd chromatography systems and in large-diameter beds. A lower bound of the axial... [Pg.1512]

For Molecular weight determination by viscometry we do not need absolute h value, viscosity measurements may be carried out in simple Ostwald Viscometer. Because of (the non-Newtonian behaviour of most macromolecular solutions at high velocity gradients in the capillary, the viscometer dimensions are chosen in such a manner that the viscosity gradient is the smallest possible. [Pg.133]

Figure 5.10 Intrinsic viscosity gradient within one PBT particle [30a]. From Buxbaum, L. H., J. Appl. Polym. Sci.,Appl. Polym. Symp., 35,59 (1979), Copyright John Wiley Sons, Inc., 1979. Reprinted by permission of John Wiley Sons, Inc. Figure 5.10 Intrinsic viscosity gradient within one PBT particle [30a]. From Buxbaum, L. H., J. Appl. Polym. Sci.,Appl. Polym. Symp., 35,59 (1979), Copyright John Wiley Sons, Inc., 1979. Reprinted by permission of John Wiley Sons, Inc.
Maxwell element or model Model in which an ideal spring and dashpot are connected in series used to study the stress relaxation of polymers, modulus Stress per unit strain measure of the stiffness of a polymer, newtonian fluid Fluid whose viscosity is proportional to the applied viscosity gradient. [Pg.480]

The mere fact that a density inversion occurs through coupled diffusion of polymer components is not a sufficient condition for the generation of instability associated with fluid motion. For example, the system may be stabilised by either fluctuations in the movements of the solute leading to dissipation of the density inversion or local viscosity gradients. [Pg.142]

According to Newton s law, the stress S is proportional to the viscosity gradient or flow dyldt. The proportionality constant is the coefficient of viscosity often referred to as simple viscosity rj, so S = t)(dy/dt). [Pg.24]

As mentioned earlier, space or Held dependent material properties can also be represented with radial functions. This is the case with rate of deformation- or velocity-dependent viscosity. Here, we present two alternatives to represent viscosity and viscosity gradients. The first and simpler form, also referred to a the direct method, simply applies the RFM to the viscosity itself as... [Pg.578]

Particle radii (R) are calculated from the sedimentation times (t) by means of the Stokes equation. For a spin fluid with density and viscosity gradients... [Pg.207]

The slower warming rate and minimization of large viscosity gradients tend to allow reaction 4 to compete better with reaction 3. Thus, solvent fragmentation/ligation (reaction 4) competes better over the slow warm-up period. [Pg.148]

Here R is termed the retention ratio and V is the void volume, that is, the volume required to elute a nonretained component. In ThFFF, corrections to equation 2 must be made to account for the viscosity gradient in the channel, which arises from the temperature gradient. The details of these corrections are lengthy and can be found in reference 13. [Pg.187]

Heat transfer for laminar flow in tubes with a parabolic velocity profile. (Does not include effects of natural convection or viscosity gradients.)... [Pg.338]

EXAMPLE A 52 API gasoline which hos a viscosity of 0.5 centi-poise at its average temperature flows through the segmentally baffled shell of an exchanger with Va O.D. tubes. The geometric mean mass velocity is 77.8 lb./(sec.) (sq. ft.) and the viscosity gradient is very close to 1. What is the shell-side heat transfer coefficient 1—Connect G<. = 77.8 and /u = 0.5 with Line 1. 2—Pivot Line 1 about its intercept on uncalibrated line until it intersects 52° API. 3—Read h.. = 184. [Pg.54]

The zeta potential of the virus at 0.02 I was measured by zonal electrophoresis in a sucrose gradient. In its evaluation we corrected the retarded, relaxed Smoluchowski equation (33) for the sucrose-dependent viscosity gradient (8). Again, the Hunter and Wright correlation was used to estimate the value of the zeta potential at 0.305 I. [Pg.112]

Both methods introduce a density and viscosity gradient between the suspension and the spin fluid. The gradient cushions the hydrodynamic shock of the particles as they enter the spin fluid and, thus, produces a smooth transition, ensures laminated flow and avoids streaming. The pros and cons of line start vs homogeneous start are well documented in the literature. Good results using the line start method are reported for the Joyce Loebl, Horiba Capa 700 and Brookhaven B1 DCP instruments. [Pg.628]


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See also in sourсe #XX -- [ Pg.157 ]




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