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Impeller high viscosity

Commonly used heat-transfer surfaces are internal coils and external jackets. Coils are particularly suitable for low viscosity Hquids in combination with turbine impellers, but are unsuitable with process Hquids that foul. Jackets are more effective when using close-clearance impellers for high viscosity fluids. For jacketed vessels, wall baffles should be used with turbines if the fluid viscosity is less than 5 Pa-s (50 P). For vessels equipped with cods, wall baffles should be used if the clear space between turns is at least twice the outside diameter of the cod tubing and the fluid viscosity is less than 1 Pa-s (10... [Pg.437]

High-Viscosity Systems A axial-flow impellers become radial flow as Reynolds numbers approach the viscous region. Blending in... [Pg.1632]

Most paste and high-viscosity mixtures are nonnewtonian, with viscosity dropping with shear rate. Consequently, increasing impeller speed may be counterproductive, as the transmitted shear drops rapidly and an isolated hole may be created in the central mass without circulation of the bulk material in the remainder of the vessel. [Pg.1643]

Slow speed close-clearance impellers are used when mixing high viscosity materials. Helical or anchor type close-clearance impellers are used in this application at speeds from 5 to 20 rpm. Table 1 compares the pow er required and cost for conventional axial flow turbines and the helical type. [Pg.207]

Paddle A paddle is similar to a turbine impeller but typically has only two large blades and operates at lower speeds than a turbine. They are primarily used in high viscosity mixing operations. In European and Japanese literature the term "paddle" also is used to describe the flat blade and pitched blade turbines discussed above. The term "turbine" generally is reserved for disk turbines. [Pg.455]

Figure 5-5D. Gate paddle impeller is designed for materials of high viscosity and operates at low shaft speeds. It is most desirable for shallow, wide tanks and wherever low shear Is a requirement. Courtesy of Lightnin (formerly Mixing Equipment Co.), a unit of General Signal. Figure 5-5D. Gate paddle impeller is designed for materials of high viscosity and operates at low shaft speeds. It is most desirable for shallow, wide tanks and wherever low shear Is a requirement. Courtesy of Lightnin (formerly Mixing Equipment Co.), a unit of General Signal.
Kneaders, Z- and sigma-blade, and Banbury mixers as shown in Figure 7.20, are generally used for the mixing of high-viscosity liquids, pastes, rubbers, doughs, and so on. The tanks are usually mounted horizontally and two impellers are often used. The impellers... [Pg.305]

The 45° axial-flow turbine is more efficient at all Reynold s numbers than the flat-blade radial turbine. However, as the pitch angle decreases below 45°, the impeller becomes increasingly sensitive to high viscosity. [Pg.80]

Apart from the critical impeller speed for solid suspension and efficient gas dispersion, flooding is also a very important phenomenon in three-phase systems. Flooding may take place at low impeller speed or high gassing rate. Under these conditions, the gas is dispersed just around the central shaft of the tank, whereas the solids are settled at the bottom. Flooding characteristics are not affected by particles. Furthermore, high-viscosity liquids are able to handle more gas before flooding than low-viscosity liquids. [Pg.135]

FIGURE 28 Typical helical flow impeller for high-viscosity blending with close clearance to the tank wall. [Pg.297]

For relatively high viscosities, the liquid itself prevents uncontrolled swirling. Therefore, when the liquid viscosity is greater than 5000 cP (5 Pa s), no baffles are required for most applications. For impellers located less than one impeller diameter from the bottom of the tank, an additional correction factor for the power number may be necessary [3]. [Pg.440]

Estimate viscous power number for the helix impeller. A helical-ribbon impeller, also called a helix impeller, is used primarily when high-viscosity fluids are being processed. Most of the power data on such impellers have been obtained in the laminar and transitional flow ranges. The effect on power of common geometry factors, i.e., impeller diameter D, tank diameter T, helix pitch P, impeller height H, and helix (blade) width W, can be incorporated into a correlation for a (dimensionless) viscous power number ... [Pg.457]

Medium/High Viscosity Blending with a 6BD Impeller... [Pg.288]


See other pages where Impeller high viscosity is mentioned: [Pg.424]    [Pg.425]    [Pg.427]    [Pg.430]    [Pg.437]    [Pg.512]    [Pg.1623]    [Pg.1643]    [Pg.2102]    [Pg.455]    [Pg.277]    [Pg.293]    [Pg.302]    [Pg.79]    [Pg.271]    [Pg.300]    [Pg.423]    [Pg.98]    [Pg.66]    [Pg.135]    [Pg.297]    [Pg.557]    [Pg.24]    [Pg.455]    [Pg.459]    [Pg.326]    [Pg.300]    [Pg.1444]    [Pg.1464]    [Pg.1859]    [Pg.284]    [Pg.2259]    [Pg.262]    [Pg.133]   
See also in sourсe #XX -- [ Pg.1254 , Pg.1255 , Pg.1308 ]




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