Ore material handling
The handling and storage of ore materials (Bulk
solids) constitutes a major function in all Mineral Beneficiation plants. The handling of Bulk solids is
required between each processing step in a plant, and often as part of a
processing step. Surge capacity or storage is also required, both ahead of the
plant and within it. As the costs of storage and handling systems in
Beneficiation plants are substantial, the storage and handling facilities
should be designed and operated with a view to obtaining maximum reliability, efficiency
and economy. Bulk solids consist essentially of many particles or granules of
different sizes (and possibly different chemical compositions and densities) randomly
grouped together to form of a bulk. The nature of such a material – that is,
its appearance, its feel, the way it behaves in various circumstances, and so
on – is thus dependent upon many factors, but principally upon the size, shape
and density of the constituent particles. The nature of bulk solids, described
in terms of appropriate characteristics is an essential consideration when
designing or selecting equipment for its handling or storage. Size, Shape and
Surface area of the particles, Density of the particles, Bulk density,
Compressibility, Cohesion and Adhesion, Angle of repose, Angle of fall, Angle
of difference, Angle of spatula, Angle of surcharge, Angle of slide, Tackiness,
Abrasion, Corrosion, Friability, Dispersability, Hygroscopicity and Moisture content,
are some of the important properties of bulk solids to be considered while
handling them. Storage and transport systems for bulk materials, slurries and water
are inevitable for beneficiation plants.
1.PROPERTIES OF BULK SOLIDS
1.1 Size of the particles
Various terms like coarse, small, fine and
superfine, are used to give a qualitative indication of the size of the particles
constituting a bulk solid. The word ‘size’
is used loosely to mean some sort of average dimension across the particle.
There are many methods of determining the particle
size distribution of bulk solids. The most popular (and cheapest) method of
particle size analysis, especially with relatively coarse materials, is
sieving. The sieve analysis method is main method for particles determining.
Sedimentation, elutriation, Optical microscopy, Coulter counter and Laser diffraction
spectrometry are some other methods.
1.2 Shape of the particles
Experience has shown that the shape of the
constituent particles in a bulk solid is an important characteristic as it has
a significant influence on their packing and flow behaviour. Flaky, needle
shaped, bulky, rounded, angular, etc. are the terms used to indicate the shape
of the particles qualitatively. Many attempts have been made to define the
shape of non-spherical particles to indicate the extent to which particles differ
from the sphere. Sphericity and the shape factor are the two terms used for the
quantitative representation of the shape of the particles.
1.3 Surface area of the particles
The specific surface is defined as the sum of the
surface areas of all particles contained in unit mass of the material. The
surface area of certain finely divided bulk materials is of considerable
importance during the processing and use of these materials. Various techniques
have therefore been devised to measure this property. The most common type of
instrument for measuring the surface area of powders and particulate materials
is the permeameter.
1.4 Particle density (Density of the bulk
solids)
The density of the particle is defined as the mass
of the particle per unit volume. The ratio of the density of the particle to
the density of water is defined as specific gravity. For a bulk material (bulk
solids), the average particle density can be determined by dividing the mass of
the material (solids) with the true volume occupied by the particles (not
including the voids).
1.5 Bulk density
The bulk solids are really a combination of
particles and space, the fraction of the total volume not occupied by the
particles is referred as the ‘voidage’ or ‘void fraction’. Sometimes
the term ‘porosity’ is applied to bulk solids to mean the same as ‘voidage’.
The particle porosity can be defined as the ratio of the volume of pores
within a particle to the volume of the particle
(inclusive of pores).
A quantity of particulate or granular material will
have an apparent density, usually termed as ‘bulk density’, which can be
defined as the mass of the material divided by its total volume (particles and
voids). Three kinds of bulk density that apply to materials handling
calculations are (1) Aerated density (2) Packed density (3)Dynamic
or Working density.
1.6 Cohesion and adhesion
Cohesion is
defined as the molecular attraction by which particles of a body or material are
united or held together. When the forces of attraction (cohesion) are low, the bulk
material can be made to flow easily under the influence of gravity with the
particles moving as individuals relative to one another. Dry sand is a familiar
example of free-flowing bulk solids. However, high inter-particle cohesive
forces may be caused by moisture or electrostatic charging in fine materials
and tend to form agglomerates so that the material flows in an erratic manner
as lumps.
Adhesion is the
sticking together or adhering of substances in contact with each other.
Cohesion is internal, adhesion is external. Adhesion describes the tendency of solid
particles to ‘stick’ to a containing surface, such as a wall of a hopper or the
side and bottom surfaces of a channel or chute. An extreme example of this is
kaolin clay, which is so tacky that it will stick to a wall when thrown against
it. This can create unusual problems in moving this material from storage.
Adhesive materials tend to bridge in storage and thus require external
assistance.
1.7 Angle of repose
Angle of repose is defined as the included angle
formed between the edge of a cone shaped pile formed by dropping the material
from a given elevation (6.8 cm – according to the standard) and the horizontal
(Figure1).
Figure 1 Angle
of repose
Angle of repose gives a direct indication of how
free flowing the material will be.Angle of repose is sensitive to the condition
of the supporting surface, the smoother the surface the smaller the angle.
Moisture tends to increase the angle of repose. Bulk solids with an Angle of
Repose between 25° and 35° are generally considered free flowing. Table 1 shows
flowability character based on angle of repose.
Table1 Flowability
character
1.8 Angle of fall
When a material lies in a pile at rest, it has a
specific Angle of Repose. If the supporting surface experiences vibrations,
impacts or other movement, the material on the sloped sides of the pile will
dislodge and flow down the slope. The new Angle of Repose that forms is
referred to as the Angle of Fall. After measuring the angle of repose, the cone
shaped pile of material is jarred by dropping a weight near it. The pile will
fall resulting in a new, shallower angle with the horizontal. This new angle of
repose is measured as angle of fall.
The way the pile falls is of special interest. If
particles fall and spread out along the slope of the pile, only the degree of
flowability is indicated. If the entire pile collapses, it indicates that the
material contained entrained air and is prone to flushing.
1.9 Angle of difference
The angle of difference is the difference between
the angle of repose and the angle of fall. The greater the angle of difference
(between angles of repose and fall) the more free flowing the material is. It
is an indirect measure of fluidity, surface area and cohesion.
1.10 Angle of spatula
The Angle of Spatula provides an indication of the
internal friction between particles. It is determined by inserting a flat blade
into a pile of granular material and lifting vertically. The new Angle of
Repose, which the material forms relative to the blade surface, is known as the
Angle of Spatula. Generally, bulk solids with an Angle of Spatula less than approximately 40° are considered
as free flowing. A highly flowable material will have an acute angle of
spatula.
1.11 Angle of surcharge
The Angle of Surcharge is defined as the included
angle formed between the edge of a cone shaped material and the horizontal when
the material is at rest on a moving surface, such as a conveyor belt. This
angle is usually 5° to 15° less than the angle of repose, though in some
materials it may be as much as 20° less. The angle of surcharge is often called
the dynamic angle of repose.
One yardstick to measure the flowability of a
particular material is by the angle of repose and angle of surcharge. The
inter-relationship is shown in Table2.
Table 2 Inter-relationship
between angle of repose, surcharge and flowability.
1.14 Abrasion
Abrasion means scraping off or wearing away.
Knowing a material’s abrasiveness is important in the proper design of
equipment to protect against wear. The materials like coke and foundry sand
will wear hoppers, chutes, screw feeders and conveyors, and pneumatic handling
systems. Hardened steels, wear resistant liners and high density plastics must
be considered for contact materials in such cases.
1.15 Corrosion
Corrosion can be defined as the deterioration of
the material and its properties due to chemical or electrochemical reaction
between a material, usually a metal, and its environment. Most metals corrode
on contact with water (and moisture in the air), acids, bases, salts, oils, and
other solid and liquid chemicals. When corrosive materials are processed, they
must be handled in equipment with contact surfaces of alloy steel, special
plastics or coated with corrosion resistant paint.
1.16 Friability
Friability means the breaking down of the particles
in to smaller pieces. If it is undesirable to have any breakdown of the product
in the process, as in coal, it is mandatory to use equipment whose design or
performance will prevent such breakage.
1.17 Dispersibility
Dispersibility is the basic property that causes a
material to flood or to produce dustiness in the surroundings. Dispersibility
indicates the dusting and flushing characteristics of a material. It is a
measure of the propensity for a granular material to form dust and thus lose
mass to the surrounding air. Dispersible materials are generally of low bulk
density and fine particle size, which causes them to behave more like a gas or a
liquid than a solid. Dispersibility and floodability are interrelated.
Materials with a dispersibility rating of more than 50% are very floodable and
are likely to flush from a storage bin unless measures are taken to prevent
this occurrence.
1.18 Moisture content and hygroscopicity
Materials that have an inherently high percentage
of moisture may pose a handling problem. Free moisture, surface moisture or
combined moisture as in wet ores cause the problems of sticking and poor flow.
Generally, free moisture over 5–10% is considered risky. Particles of high
porosity pick up and retain moisture and pose problems. Likewise, those materials
that are hygroscopic or absorb moisture will cake and refuse to flow.
2 STORAGE
The following are the main purposes of ore storage:
1 To receive ore intermittently and deliver it
smoothly.
2 To accumulate mill products for intermittent
disposal.
3 To maintain an adequate tonnage of ore for treatment.
4 To smooth out irregularities in working (surge
storage).
5 To facilitate balanced blending of dissimilar
minerals
Storage is accomplished in stock piles, bins, tanks
and ponds.
Stockpiling is
defined as the storage of dry bulk material in piles on the ground and is
adopted to store coarse material of low value at outdoors, especially if the
duration of storage is extensive. Stockpiles are formed on a concrete or
earthen pad. Fixed, traveling and radial stackers, tripper and shuttle
conveyors are used to form stockpiles.
Cyclic machines such as grab bucket, dragline and
shovel, continuous machines such as drum, rake and bucket wheel are used for
reclaiming the stock piles. Stacker/re-claimers are also available to perform
both functions.
Bins,
Silos and Bunkers are used for dry or
filtered materials where the storage period is short. A bin is a container of
cylinder and hopper sections for bulk solids with one or more outlets for withdrawal
either by gravity alone or by gravity assisted by flow promoting devices such
as feeders. Silos, bunkers and other specialized terms used in various
industries are also bins. A Silo has large cylindrical section whereas a Bunker
has short cylindrical section.
Tanks, usually
with an agitator, are employed for storing pulps and slurries.
Ponds and Dams are
used for storing water and tailing slurries.
3 CONVEYING
The ore is transported by wagon, truck, rope
haulage, aerial tramway etc., from mine to beneficiation
plant. Within the mill, the ore is transported by gravity and by conveyors.
Gravity transport is the
flow of material in which actuating force is gravity and is carried out in
chutes and launders. Chutes are
steeply inclined troughs of rectangular sections for the gravity transport of
dry solids. Launders are
gently sloping troughs of rectangular, triangular or semicircular sections for
the gravity transport of suspensions of ore or mineral.
Conveyors are
used to transport the ore when the horizontal distance is relatively short.
There is no arbitrary limit beyond which a conveyor system cannot be used. Travel
may be horizontal or inclined either up or down, the maximum practicable inclination
varies with the type of conveyor and the nature of materials.
A Belt conveyor, the most versatile and
widely used type, consists of an endless belt running around head and tail
pulleys and resting on various kinds of idlers at intervals along both its
upper and return runs. Drive is generally through the head pulley
Pan conveyors are
similar to belt conveyors in method of drive and support, but differ in that
the carrying surface consists of a series of articulated plates or shallow pans
supported on rollers and tied together by pins.
A Vibrating conveyor consists of a
material-transporting trough driven by a vibrator.
A Flight conveyor is essentially a trough
through which a series of scrapers attached to chain or rope is drawn.
An En masse conveyor conveys materials by
causing them to flow in a compact and unbroken stream through a conduit.
A Screw conveyor consists of a spiral blade
attached to a revolving shaft which pushes the material along the bottom of a
semicircular trough.
A Bucket conveyor consists of an endless
belt or chain with buckets attached, running upon two pulleys or sprocket
wheels, one above and one below. The belt or chain travels vertically or at a
steep angle.
Skip hoists are
widely used to haul ore from underground mines and to elevate coarse bulk
materials over a limited distance. They provide an intermittent flow of material.
Pneumatic and Slurry
transport are the methods of transporting material using air and water as
the transporting medium respectively. Material to be transported is usually in
powdered form and is transported through a pipeline system by utilizing the kinetic
energy of the fluid (air/water) to move the material. This kinetic energy to
the fluid is imparted by a blower or vacuum pump in the case of pneumatic
transport and by a reciprocating or centrifugal pump in the case of slurry
transport.
4 FEEDERS
Feeding is essentially a conveying operation in
which the distance traveled is short and in which close regulation of the rate
of passage is required. The feeder is installed at the outlet of a bin, silo or
bunker. The different types of feeders are chain feeder, apron feeder, pan feeder,
belt feeder, roller feeder, rotary feeder, reciprocating-plate feeder, plunger
feeder, revolving-disk feeder, and vibrating feeders.
5 DISPOSAL OF PRODUCTS
The concentrated product from a beneficiation plant
is transported through wagons, trucks, conveyors, and pipelines for further
processing. The methods for disposal of tailings include discharge of tailing
into rivers and streams, dumping of coarse tailings on to land, re-using
tailings for some purpose, filling of mined-out areas etc. The disposal of
tailings is a major environmental problem. It leads to pollution which is of
major concern to the public and government. Uncontrolled discharge of tailings is
no longer tolerated. One has to follow environmental legislation laid down by
the government before the tailings are disposed of.
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