Page 383 - Chemical Process Equipment - Selection and Design

346 DISINTEGRATION, AGGLOMERATION, AND SIZE SEPARATION OF PARTICULATE SOLIDS

AHFlywheel
Feed

F/ywhee/

/Relief
spring

Discharge

(b)

C ~ 650 fprn ~400 fprn 250 fprn ~ ~ ~ ~ )
~

?&-in. ball 2L5-in. ball
crushing crushing
I-in. material %-in. material
=43:1 = 125:l

111 ion
& Periphval tlischnrge 4 discharge
when required
(e) (f 1
Figure 12.5. Jaw, roll, impact, and tumbling equipment for size reduction. (a) Blake-type jaw crusher operates at 200-300 strokes/min
(Allis-Chalmers Co.). (b) Smooth roll crusher, for which operating data are in Table 12.8(b). (c) Swing hammer mill; operating data in Table
12.7(a). (d) View of a conical ball mill, showing distributions of balls and material and crushing ranges; data in Table 12.6(b) (Hardinge Co.).
(e) Tube mill with three compartments, length to diameter ratio 3-5. (f) Rod mill in a cylindrical tumbler, LID = 1.2-1.6; data in Table
12.6(d).