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Centrifugal Pumps Design and Application 2nd ed - Val S. Lobanoff, Robert R. Ross (Butterworth-Heinemann, 1992)

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244 <strong>Centrifugal</strong> <strong>Pumps</strong>: <strong>Design</strong> <strong>and</strong> <strong>Application</strong><br />

Figure 13-11. (A) Typical performance characteristic of nonsettling slurries; |B)<br />

typical performance characteristic of settling slurries.<br />

go over 100% in badly controll<strong>ed</strong> systems. For this reason large margins<br />

are built into the design of slurry pumps <strong>and</strong> motors. Usually the motor is<br />

mount<strong>ed</strong> above the pump on an adjustable frame (belt adjustment) to save<br />

space <strong>and</strong> to safeguard against flooding. (Refer to Figure 13-10.)<br />

The Effect of Slurries on Pump Performance<br />

When centrifugal pumps are requir<strong>ed</strong> to h<strong>and</strong>le slurries, it is st<strong>and</strong>ard<br />

practice to publish pump performance curves bas<strong>ed</strong> on clear water performance.<br />

Therefore, to pr<strong>ed</strong>ict the performance of pumps h<strong>and</strong>ling slurries<br />

of different characteristics, correction factors are appli<strong>ed</strong>.<br />

When h<strong>and</strong>ling slurries, the pump performance is mainly affect<strong>ed</strong> by<br />

the solid particle diameter, specific gravity, <strong>and</strong> concentration. Very fine<br />

particles in a slurry can be "nonsettling" <strong>and</strong> cause it to behave as a homogeneous<br />

Newtonian liquid with an "apparent" viscosity. Slurries with<br />

very fine solids in suspension (usually less than 100 microns) will retain<br />

liquid-like characteristics at volumetric concentrations very near to the<br />

limiting voidage, <strong>and</strong> limits are relat<strong>ed</strong> only to the effects of high viscosity.<br />

Figure 13-1 la shows typical nonsettling slurry pump characteristics.

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