Tumbling Mill Grinding Devices
The
various mining machine including grinding devices used in the industry are distinguished in terms of the
manner by which energy is introduced into the system and in terms of capacity
and particle transport into and out of the mill. Each device is characterized
with respect to particle size range, design relationships, wear, and efficiency
of energy utilization. For some grinding devices, well-defined design
relationships have not been established, and in these cases detailed data on
typical installations are given when available.
Similarly,
wear data for some grinding devices are not always available, especially for
the more recently developed mills that have not been used extensively on an
industrial scale. In addition, the wear characterization is difficult to
generalize because it is highly dependent both on the nature of the feed and
the materials of construction. The efficiency characterization is the
free-crushing efficiency and represents that portion of the total energy
consumption that would be required for single-particle fracture under slow
compression.
Intermediate
and fine size reduction by grinding is frequently achieved in a ball mill in which
the length of the cylindrical shell is usually 1 to 1.5 times the shell
diameter. Ball mills of greater length are termed “tube mills,” and when hard
pebbles rather than steel balls are used for the grinding media, the mills are
known as “pebble mills.” In general, ball mills can be operated either wet or
dry and are capable of producing products on the order of 100 μm. This duty represents reduction ratios as great as 100.
The ball
mill, an intermediate and fine-grinding device, is a tumbling drum with a 40%
to 50% filling of balls (usually steel or steel alloys; Figure1). The material
that is to be ground fills the voids between the balls. The tumbling balls
capture the particles in ball/ball or ball/liner events and load them to the
point of fracture. Very large tonnages can be ground with these devices because
they are very effective material handling devices. The feed can be dry, with
less than 3% moisture to minimize ball coating, or a slurry can be used
containing 20% to 40% water by weight. Ball mills are employed in either
primary or secondary grinding applications. In primary applications, they
receive their feed from crushers, and in secondary applications, they receive
their feed from rod mills, autogenous mills, or semiautogenous mills. Regrind
mills in mineral processing operations are usually ball mills, because the feed
for these applications is typically quite fine. Ball mills are sometimes used
in single-stage grinding, receiving crusher product. The circuits of these
mills are often closed with classifiers at high-circulating loads.
Fig1. Cutaway of ball mill with chute
feeder and grate discharge
There are
three principal forms of discharge mechanism. In the overflow ball mill, the
ground product overflows through the discharge end trunnion. A diaphragm ball
mill has a grate at the discharge end (Figure 1). The product flows through the
slots in the grate. Pulp lifters may be used to discharge the product through
the trunnion, or peripheral ports may be used to discharge the product.
The mill
liners used are constructed from cast alloy steels, wear-resistant cast irons,
or polymer (rubber) and polymer metal combinations. The mill liner shapes often
recommended in new mills are double-wave liners when balls less than 2.5 in.
are used and single-wave liners when larger balls are used. Replaceable metal
lifter bars are sometimes used. End liners are usually ribbed or employ replaceable
lifters.
The
typical mill-motor coupling is a pinion and gear. On larger mills two motors
may be used, and in that arrangement two pinions drive one gear on the mill.
Synchronous motors are well suited to the ball mill, because the power draw is
almost constant. Induction, squirrel cage, and slip ring motors are also used.
A high-speed motor running 600 to 1,000 rpm requires a speed reducer between
the motor and pinion shaft. The “gearless” drive has been installed at a number
of locations around the world.
Autogenous/Semiautogenous Mills
Autogenous
and semiautogenous mills represent a relatively new type of tumbling mill that,
under certain conditions, can replace size reduction equipment used for
secondary crushing as well as primary and final grinding. Basically, the
breakage mechanism is similar to that found in other tumbling mills. The unique
feature of this device is that the coarse ore particles themselves are used as the
grinding media, not unlike a pebble mill in which the pebbles are generated
naturally from the ore body. In this regard, autogenous grinding is to be
applied to ores with necessary characteristics.
The
autogenous mill itself is a coarse-grinding device, consisting of tumbling drum
with a 25% to 40% volume filling of ore. Metallic or manufactured grinding
media is not used. Autogenous mills are fed run-of-mine ore or primary crusher
product that is –10 in. Inside the mill, large pieces break into smaller pieces a few inches
in size. These natural pebbles act as the grinding media in the autogenous
mill. The main modes of breakage are thought to be impact breakage and
abrasion.
Semiautogenous
milling results when a small amount of steel balls, 3% to 20% of mill volume,
is added to the mill charge. The addition of a small ball charge to an
autogenous mill changes the nature of the mill performance considerably. In
this case, major design modifications may be required to carry the additional
charge. Generally, the addition of a ball charge increases the mill capacity
significantly but increases operating costs for balls and power (Figure 2).
Fig2. Semiautogenous mill
Many
circuit configurations are possible, but essentially the autogenous mill is
operated as a single-stage primary mill, or it can be followed by secondary
pebble or ball milling. The autogenous mill is often operated in closed circuit
with a trommel screen or external vibrating screen classifying the discharge.
Circulating loads are low compared with those in ball mill circuits, because
autogenous mills do not benefit from high-circulating loads in the same way
ball mills do. Intermediate crushers are sometimes used to crush the largest
pieces in the recycle stream.
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