Particle vortex

Fig. 9. Bubble-wake interactions in a gas—Hquid-soHd reactor (a) soHds concentration profile within bubble-wake domain, where A—A and B—B represent planes through the bubble, vortex, and wake (b) projected impact of interactions on reaction rate as function of particle si2e and Hquid velocity, where (—)...

Cyclone Separators Cyclone separators are described in Chapter 7. Typically used to remove particulate from a gas stream, the gas enters tangentially at the top of a cylinder and is forced downward into a spiral motion. The particles exit the bottom while the gas turns upward into the vortex and leaves through the top of the unit. Pressure drops through cyclones are usually from 13 to 17 mm water gauge. Although seldom adequate by themselves, cyclone separators are often an effective first step in pollution control. 

The rotational operation of a CFB leads to a vortex motion in the freeboard which tends to inhibit particle loss by elutriation. Because of the relatively compact nature of the CFB and the operating flexibility provided by the rotational motion, the CFB has been proposed for a variety of applications including coal combustion, flue gas desulfurization, gas combustion, coal liquefaction and food drying. 

In order to reduce the influence ol unfavorable stagnation regions and vortex structures with their risk for accumulation of contaminants, tests should be carried out to characterize the functioning of the bench. In connection with these tests, induction tests should also be performed. Here smoke (particles) generated outside the bench and the probe of a particle counter placed inside the bench in the critical regions can give valuable information. 

The vortex exhaust has a geometry that generates a rotating flow behind the opening. It is suitable for installation in a narrow space and it is traditionally used with hand-held equipment producing jets of air and particles. This type of exhaust opening is also called a tornado exhaust or a cyclone exhaust. 

Normally the vortex finder should extend down into the conical portion of the cyclone. It is thought that the vortex finder plays an important role in the maintenance of a stable spiraling fluid flow in the cyclone, and this makes it more difficult for the particles to leak through the boundary layer on the roof of the lid of the cyclone to the overflow tube.- Without a vortex finder, the efficiency may be reduced by 4-5%. However, an excessive long vortex finder may hinder the high spin velocity in the fluid flow and thus reduce the efficiency of the cyclone. 

Fluid mixing and particle suspension in unbaffled vessels (Figure 7.1(a)) may be poor, experiencing vortexing but this can be improved by the addition of wall... 

The unit shown in Figure 4-49 has been used in many process applications with a variety of modifications [18,19,20]. It is effective in liquid entrainment separation, but is not recommended for solid particles due to the arrangement of the bottom and outlet. The flat bottom plate serves as a protection to the developing liquid surface below. This prevents re-entrainment. In place of the plate a vortex breaker type using vertical cross plates of 4-inch to 12-inch depth also is used, (Also see Reference [58].) The inlet gas connection is placed above the outlet dip pipe by maintaining dimension of only a few inches at point 4. In this type unit some liquid will creep up the walls as the inlet velocity increases. 

Vertical side-W all baffles (Figures 5-23B and C and 5-34) projecting about Ko to K of the tank diameter into the v essel perform a helpful purpose in controlling vortex action. The baffles are set off from the tank w all a few inches to prev ent build-up of particles. 

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