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Solid moving

In our discussion so far we have begged the question of just how the atoms in a solid move around when they diffuse. There are several ways in which this can happen. For simplicity, we shall talk only about crystalline solids, although diffusion occurs in amorphous solids as well, and in similar ways. [Pg.185]

Although we include adsorption here following the chapter on mass transfer, we should be clear that it is a very specific process in its fullest fundamental meaning. Adsorption is the process by which molecules in the fluid phase in contact with a solid move to the solid surface and interact with it. Once at the solid surface these molecules may be reversible or irreversible adsorbed, that is, they may come back off the surface to the fluid phase with their full molecular integrity intact, or they may be so strongly bound that the rate of removal is for all purposes close enough to zero to be considered zero. [Pg.249]

Electrostatic Properties of Solids in Suspension. Some solids in suspension will migrate from one pole to another when placed between direct current electrodes. The phenomenon of solids moving toward an electrode is known as cataphoresis. [Pg.167]

Diffusion is a physical phenomenon, which occurs when the atoms of a solid move into another solid above a certain temperature. Diffusion is particularly pronounced with silicon into aluminum, as mentioned in Sec. 2.2 above. It occurs during subsequent processing steps when the temperature exceeds 400°C. [Pg.376]

Solids Circulation Pattern. Yang et al. (1986) have shown that, based on the traversing force probe responses, three separate axial solids flow patterns can be identified. In the central core of the bed, the solid flow direction is all upward, induced primarily by the action of the jets and the rising bubbles. In the outer regions, close to the vessel walls, the solid flow is all downward. A transition zone, in which the solids move alternately upward and downward, depending on the approach and departure of the large bubbles, was detected in between these two regions. [Pg.296]

In 1998 the auto industry moved from weak commitments to a solid move toward fuel cells and fuel cell vehicles. All the auto companies began pursuing hydrogen fuel cells in some way. [Pg.133]

In 1998 the auto industry turned from weak commitments to a solid move toward fuel cells and EVs. All the auto companies are pursuing hydrogen fuel cells in some way. But, the new cars on the road in the near future are likely to be a mix of vehicles including those with electric drive, including battery EVs, hybrids with gasoline and direct-injection diesels, turbo generators and fuel cells. [Pg.181]

The earliest application of a moving bed in which solids moved with respect to the containing vessel was reported in the late 1940s. A typical application was the recovery of ethylene from gas composed mainly of hydrogen and methane, and with some propane and butane. The unit shown diagrammatically in Figure 17.26, taken from the work of Berg(45), is known as the hypersorber. [Pg.1028]

Note that plots, such as Figure 5.1, provide information only on the net outcome of chemical reactions. In the case of iron, a small addition does take place in estuaries as a result of desorption of Fe from the surfaces of riverine particles. As these solids move through the estuarine salinity gradient, the major cation concentrations increase and effectively displace the iron ions from the particle surfeces. Since this release of iron is much smaller than the removal processes, the net effect is a chemical removal of iron. Sedimentation of these iron-enriched particles serves to trap within estuaries most of the riverine transport of reactive iron, thereby preventing its entry into the oceans. [Pg.103]

The HIPS resin was extruded at screw speeds of 30, 60, and 90 rpm at barrel temperatures of 200, 220, and 240 °C for Zones 1, 2, and 3, respectively. The screw temperatures in Zone 3 as a function of time at the screw speeds are shown in Fig. 10.20. Because the RTDs were positioned within 1 mm of the screw root surface, they were influenced by the temperature of the material flowing in the channels. Prior to the experiment, the screw was allowed to come to a steady-state temperature without rotation. Next, the screw speed was slowly increased to a speed of 30 rpm. The time for the screw to reach a steady state after changing the screw speed to 30 rpm was found to be about 10 minutes. The temperature of the T12 and T13 locations decreased with the introduction of the resin. This was caused by the flow of cooler solid resin that conducted energy out from the screw and into the solids. At sensor positions downstream from T13, the screw temperature increased at a screw speed of 30 rpm, indicating that the resin was mostly molten in these locations. These data suggest that the solid bed extended to somewhere between 15.3 and 16.5 diameters, that is, between T13 and T14. When the screw speed was increased to 60 rpm, the T12 and T13 sensors decreased in temperature, the T14 sensor was essentially constant, and the T15, T16, and T17 sensor temperatures increased. These data are consistent with solids moving further downstream with the increase in screw speed. For this case, the end of the solids bed was likely just upstream of the T14 sensor. If the solid bed were beyond this location, the T14 temperature would have decreased. Likewise, if the solid bed ended further upstream of the T14 sensor, the temperature would have increased. When the screw speed was increased to 90 rpm, the T12, T13, and T14 temperatures decreased while the T15, T16, and T17 temperatures increased. As before, the solids bed was conveyed further downstream with the increase in screw speed. At a screw speed of 90 rpm, the solid bed likely ended between the T14 and T15 sensor positions, that is, between 16.5 and 17.8 diameters. These RTDs were influenced by the cooler solid material because they were positioned within 1 mm of the screw root surface. [Pg.450]

Isaac s theory explained the facts beautifully, but it was wrong. Even geniuses have their off days.That s important to remember because there are times when something seems to fit the facts perfectly, but you may not have all of the facts.That was the case for Isaac no one had all of the facts yet. Later experiments have shown that all molecules are always moving (even molecules in solids move by vibrating) and that they are attracted to each other.The reason the pressure increases when a gas is compressed inside a container is because the molecules crash into a different part of the container much more frequently. [Pg.78]

We can achieve conversion beyond equilibrium in a reaction Such as this and run continuously by using a moving bed of chromatographic and catalytic solid. We assume that the fluid flows with a velocity Mfluid, while the solid moves upstream at a velocity Msolid- we adjust these velocities with respect to the velocities of the reactant and products, then a product that is strongly adsorbed can be made to move backwards in the tube. [Pg.511]

Semiclosed systems for handling solids often involve the use of big bags or tote bins. In these systems the solid is shipped in alarge (>1 t) container which is then lifted into place over a closed hopper or feed mechanism and a sealed connection is made. It is sometimes necessary to rap or agitate the big container to keep the solid moving and this action can result in deterioration or damage to the container or seals with consequent leaks. Also, there is some release of solids when containers are connected or disconnected as well as opportunities for dust generation. [Pg.105]

When examining eqn. (6.276) it is clear that the only two unknowns are the speed at which the solid moves, Usy, and the melt film thickness, 6. To solve for melt film thickness we can perform a energy balance by setting the heat conduction through the thickness of the film equal to the heat of fusion of the melting material and the energy required to raise its temperature from T0 to Tm... [Pg.318]

As mentioned, the flow rate in a standpipe depends on the solid feed device as well as the flow control valve. In this section, we discuss the gas-solid flows in a simple standpipe system where the feed device is a mass flow hopper and the solid flow regulator is a discharge orifice [Chen et al., 1984]. As shown in Fig. 8.15, the entrance of the vertical standpipe is connected to a conical hopper feeder of half angle solids flow patterns are considered. One is a dilute suspension flow, and the other is a solid moving bed. In this case, the following additional assumptions are needed ... [Pg.354]

Fig. 4.12 Force balances on a differential element of solids in Fig. 4.11. (a) Stationary solids F0 > Fl (b) Stationary solids, F0 < FL (c) Solids move at constant velocity in the positive x direction, (d) Solids move at constant velocity in the negative x direction. Fig. 4.12 Force balances on a differential element of solids in Fig. 4.11. (a) Stationary solids F0 > Fl (b) Stationary solids, F0 < FL (c) Solids move at constant velocity in the positive x direction, (d) Solids move at constant velocity in the negative x direction.
Finally, we comment on residence distribution in plasticating extruders. Tracer measurement will indicate a relatively narrow RTD, because the solid moves as a plug and the RTD of the melt pool is quite narrow as well, as discussed earlier. But what matters for polymers is the RTD in a molten state. This, as shown by Lidor and Tadmor (24), may be quite wide, as is the SDF. [Pg.504]

In electrophoresis the solid moves in a liquid phase due to the application of an electric field. The forces acting on the particles are similar to those that act on solvated ions ... [Pg.66]

For fine Geldart Group C powders that defluidize slowly, it has been shown experimentally that solids continued to be transported through the downcomer even when the fluidizing gas to the dipleg was turned off. The particulate solids move in the dense phase. This operation will be designated self-flow (Kwauk, 1974a). Under this condition, the total gas rate is zero ... [Pg.287]

Atoms in crystalline solids move under well-defined, allowed phase relations, the vibrational modes of the crystal. Only movements of atoms are allowed that are parallel or perpendicular to the wave vector,... [Pg.48]

The centrifuge contains a stack of conical disks spaced between 0.5 and 2 mm apart. The feed is supplied through a pipe to the center of the bowl at the base of the machine and is distributed into many thin layers. The different phases therefore have only a very short distance to travel to free themselves from each other. Once the solids have contacted the underside of the disks, the settling process is over and the solids move to the periphery of the disks, where they are thrown off the edge onto the bowl wall. [Pg.646]


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