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Machinery for Crushing and
        Grinding
Stag Jaw Crusher

 The Stag jaw crusher has a fixed jaw and a moving jaw
    pivoted at the top
   Crushing faces are formed of manganese steel.
   The max movement of the jaw is at the bottom; so there
    is little tendency for the machine to clog, though some
    uncrushed material may fall through and have to be
    returned to the crusher.
   The maximum pressure is exerted on the large material
    which is introduced at the top.
   One of the toggle plates in the driving mechanism is
    made relatively weak so that, if any large stresses are set
    up, this is the first part to fail.
   Easy renewal of the damaged part is then possible.
Stag Jaw Crusher
Stag Jaw Crusher
Stag Jaw Crusher

 The speed of operation should not be so high that a large
    quantity of fines is produced
   The angle of nip, the angle between the jaws, is usually
   about 30◦.
   Because the crushing action is intermittent, the loading
    on the machine is uneven and the crusher therefore
    incorporates a heavy flywheel.
   The power requirements of the crusher depend upon size
    and capacity and vary from 7 to about 70 kW,
   the latter figure corresponding to a feed rate of 10 kg/s.
Dodge Jaw Crusher

 The moving jaw is pivoted at the bottom.
 The minimum movement is thus at the bottom and a
  more uniform product is obtained
 Although the crusher is less widely used because of
  its tendency to choke.
 The large opening at the top enables it to take very
  large feed and to effect a large size reduction.
 This crusher is usually made in smaller sizes than the
  Stag crusher, because of the high fluctuating stresses
  that are produced in the members of the machine.
Dodge Jaw Crusher
Dodge Jaw
Crusher
Both Crushers employs
a compressive force for
size reduction
Gyratory Crusher
Gyratory Crusher

 Crushing head is in the form of a truncated
    cone, mounted on a shaft
   The crushing action takes place round the whole of the
    cone
   The crusher is continuous in action, thus fluctuations in
    the stresses are smaller than in jaw crushers and the
    power consumption is lower.
   It also does not take such a large size of feed as a jaw
    crusher, although it gives a rather finer and more
    uniform product.
   Because the capital cost is high, the crusher is suitable
    only where large quantities of material are to be handled.
   Employs a compressive force for size reduction
Other Coarse Crushers – Coal Breaker

 Consists of a large hollow cylinder with perforated
    walls.
   Feed is introduced at the top.
   The cylinder is rotated and the coal is lifted by means
    of arms attached to the inner surface and then falls
    against the cylindrical surface.
   The coal breaks by impact and passes through the
    perforations as soon as the size has been sufficiently
    reduced.
   This type of equipment is less expensive and has a
    higher throughput than the jaw or gyratory crusher.
Rotary Coal Breaker
Intermediate Crushers
Edge Runner Mill
Edge Runner Mill
Edge Runner Mill

 It has heavy cast iron or granite wheel, or muller
  mounted on a horizontal shaft which is rotated in a
  horizontal plane in a heavy pan.
 Alternatively, the muller remains stationary and the
  pan is rotated
 Material is fed to the centre of the pan and is worked
  outwards by the action of the muller, whilst a scraper
  continuously removes material that has adhered to
  the sides of the pan, and returns it to the crushing
  zone.
Edge Runner Mill

 In many models the outer rim of the bottom of the
  pan is perforated, so that the product may be
  removed continuously as soon as its size has been
  sufficiently reduced.
 The mill may be operated wet or dry and it is used
  extensively for the grinding of paints, clays and
  sticky materials.
Hammer Mill
Hammer Mill

 Type of Impact mill with high speed rotating disc, to
    which are fixed a number of hammers
   Hammers are swung outwards by centrifugal force.
   Material is fed in, either at the top or at the centre, and it
    is thrown out centrifugally and crushed by hammer
    bars, or against breaker plates fixed around the periphery
    of the cylindrical casing.
   The material is beaten until it is small enough to fall
    through the screen at the lower portion of the casing.
   Hinged hammers: the presence of any hard material does
    not damage to equipment.
Hammer Mill

 The bars are replaced when they are worn out.
 Suitable for the crushing of both brittle and fibrous
 materials
       For fibrous materials it employs a screen with cutting edges.
 Suitable for hard materials
 Since a large amount of fines is produced, pressure
 lubrication is recommended for bearings.
Hammer Mill

 The size of the product is regulated by the size of the
  screen and the speed of rotation.
 In some cases the hammer bars are rigidly fixed in
  position.
 Since a large current of air is produced, the dust
  must be separated in a cyclone separator or a bag
  filter.
Laboratory Hammer Mill
Pin-type Mill
Pin-type Mill

 Two vertical steel plates
 Horizontal projections at their near faces
 One disc may be stationary whilst the other disc is
 rotated at high speed;
    or the two may be rotated in opposite directions
 The material is gravity fed in through a hopper or air
  and is thrown outwards by centrifugal action and
 broken against of the projections before it is
  discharged to the outer body of the mill
Pin type Mill

 Discharged material falls under gravity
 The mill gives a fairly uniform fine product with little
  dust
 Used with chemicals, fertilisers and other materials
  that are non-abrasive, brittle or crystalline.
 Control of the size of the product is effected by
  means of the speed and the spacing of the
  projections
 and a product size of 20 μm is readily attainable.
Single Roll Crusher
Single Roll Crusher

 Consists of a toothed crushing roll
 Roll rotates close to a breaker plate.
 The material is crushed by compression and shearing
  between the two surfaces.
 It is used extensively for crushing coal.
Single Roll Crusher
Crushing Rolls
Crushing Rolls

 Two rolls, one in adjustable bearings, rotate in opposite
    directions
   The clearance between them can be adjusted according
    to the size of feed and the required size of product.
   Protected, by spring loading, against damage from very
    hard material.
   Both rolls may be driven, or one directly and the other by
    friction with the solids.
   Effect a small size reduction ratio, 4 : 1 in a single
    operation
   commonly a no. of pairs of rolls are employed in series
         one above the other
Crushing Rolls

 Roll shells with either smooth or ridged surfaces are
 held in place

    See Ex. 2.2
Symons Disc Crusher
Symons Disc Crusher

 Has 2 saucer-shaped discs mounted on horizontal
  shafts of which one is rotated
 The two crushing faces continuously approach and
  recede.
 Material is fed in the centre between the two discs
 The product is discharged by centrifugal action as
  soon as it is fine enough to escape through the
  opening between the faces.
Fine Crushers
Buhrstone mill
Buhrstone mill

 Grinding takes place between two heavy horizontal
    wheels, one of which is stationary and the other is driven.
   The surface of the stones is carefully dressed so that the
    material is continuously worked outwards from the
    centre of the circumference of the wheels.
   Size reduction takes place by a shearing action between
    the edges of the grooves on the two grinding stones.
   Used for the grinding of
    grain, pigments, harmaceuticals, cosmetics and printer’s
    ink,
   Although used where the quantity of material is very
    small.
Roller Mill

 The roller mill consists of a pair of rollers that rotate
  at different speeds in opposite directions.
 one of the rollers is held in a fixed bearing whereas
  the other has an adjustable spring-loaded bearing
 since the rollers rotate at different speeds, size
  reduction is effected by a combination of
  compressive and shear forces.
 The roller mill is extensively used in the flour milling
  industry and for the manufacture of pigments for
  paints.
Roller Mill
Centrifugal Attrition Mills

 Babcock Mill
 The Lopulco mill or ring-roll pulveriser.
 The NEI pendulum mill.
Szego grinding mill
Szego grinding mill

 A planetary ring-roller mill
 stationary, cylindrical grinding surface with a no. of
  grooved rollers rotate.
 Connected to the central drive shaft; they are pushed
  outward by centrifugal force and roll on the grinding
  surface.
 The material is fed by gravity is discharged at the
  bottom of the mill.
Szego grinding mill

 The particles, upon entering the grinding section, are
  repeatedly
 crushed between the rollers and the stationary
  grinding surface.
 Crushing and shearing force caused by rotational
  motion of the rollers.
Ball Mill

 Consists of a rotating hollow cylinder, partially filled
    with balls
   Horizontal or at a small angle to the horizontal.
   The outlet is normally covered with a coarse screen
    to prevent the escape of the balls
   Balls fall on the grinding medium from a height
   Size reduction mainly by Impact, Compression and
    Attrition
Ball Mill
Ball Mill

 Inner surface of the cylinder is lined with an abrasion-
    resistant material
         such as manganese steel, stoneware or rubber.
 Balls occupy a volume b/n 30 and 50 per cent of total
    volume of the mill
   Balls wear out during grinding and are replaced
   Different sized balls may be used
   large balls deal effectively with the feed and the small
    ones are responsible for giving a fine product.
   For very fine grinding in small mills pebbles are often
    used instead of balls.
Compound Ball Mill

 Cylinder is divided into compartments by vertical
    perforated plates.
   Material flows axially along the mill
   Can pass from one compartment to the next only when
    its size has been reduced to less than the perforations in
    the plate.
   Each compartment is supplied with balls of a different
    size.
   large balls are at the entry while the small balls before
    discharge.
   Results in economical operation and the formation of a
    uniform product.
Wet grinding in Ball Mill

 Power consumption is generally about 30 per cent
  lower than that for dry grinding
 Continuous removal of product as it is formed is
  facilitated
Factors affecting the size of the product

 The rate of feed.
       With high rates of feed, less size reduction is effected
 The properties of the feed material.
     The larger the feed the larger is the product
     A smaller size reduction is obtained with a hard material.

 Weight of balls.
     A heavy charge of balls produces a fine product.
     The weight of the charge can be increased, either by increasing the
      number of balls, or by using a material of higher density
Factors affecting the size of the product

 Diameter of the balls.
     Small balls facilitate the production of fine material
     But do not deal so effectively with the larger particles in the feed.
      The
     For an economical operation, the smallest possible balls should be
      used.
 The slope of the mill.
     An increase in the slope of the mill increases the capacity
     But a coarser product is obtained.

 Discharge freedom.
       same effect as increasing the slope.
Factors affecting the size of the product

 The speed of rotation of the mill– Critical Speed
 Low speeds of rotation, the balls simply roll over one
    another and little crushing
   At still higher speeds they are thrown greater distances
   At very high speeds, the balls are carried right round in
    contact with the sides of the mill and little relative
    movement or grinding takes place again.
   The minimum speed at which the balls are carried round
    in this manner is called the critical speed of the mill
   Hence at Critical speed there will be no resultant force
    acting on the ball when in the uppermost position
Factors affecting the size of the product

 At critical speed the centrifugal force will be exactly
  equal to the weight of the ball.
 If the mill is rotating at the critical angular velocity ω
 rω2 = g




 Nc is the no. of revolutions per unit time
 It is found that the optimum speed is between one-
 half and three-quarters of the critical speed.
Ball mill at correct Critical speed
Factors affecting the size of the product

 The level of material in the mill.
 Power consumption is reduced by maintaining a
  low level of material
 can be done by providing suitable discharge opening
  for the product.
 If the level of material is raised, the cushioning
  action is increased and power is wasted by the
  production of an excessive quantity of undersize
  material.
Advantages of the Ball Mill

 The mill may be used wet or dry
 The costs of installation and power are low.
 The ball mill may be used with an inert atmosphere
    and therefore can be used for the grinding of
    explosive materials.
   The grinding medium is cheap.
   The mill is suitable for materials of all degrees of
    hardness.
   It may be used for batch or continuous operation.
   It may be used for open or closed circuit grinding.
Tube Mill

 Similar to ball mill
 However, length to the diameter is usually 3 or 4 :
  1, as compared with 1 or 1.5 : 1 for the ball mill.
 The mill is filled with pebbles
 The characteristics of the two mills are similar
 But material remains longer in the tube mill because
  of its greater length, and a finer product is therefore
  obtained.
Rod Mill

 High carbon steel rods about 50 mm diameter and extending
    the whole length of the mill are used.
   This mill gives a very uniform fine product
   Power consumption is low
   Not suitable for very tough materials and
   Feed should not exceed about 25 mm in size.
   It is particularly useful with sticky materials which would hold
    the balls together in aggregates, because the greater weight
   of the rods causes them to pull apart again.
   Worn rods must be removed from time to time and replaced
    by new ones, which are rather cheaper than balls.
Hardinge Mill

 A ball mill in which the balls segregate themselves
  according to size.
 The main portion of the mill is cylindrical as in the
  ball mill, although the outlet end is conical and
  tapers towards the discharge point
 large balls collect in the cylindrical portion while the
  smaller balls, in order of decreasing size,
 Like a Compound Ball Mill
Hardinge Mill
Hardinge Mill

 The mill has an advantage over the compound ball mill in
  that the large balls are raised to the greatest height and
  therefore are able to exert the maximum force on the
  feed.
 As the size of the material is reduced, smaller forces are
  needed to cause fracture and it is therefore unnecessary
  to raise the smaller balls as high.
 The capacity of the Hardinge mill is higher than that of a
  ball mill of similar size and it gives a finer and more
  uniform product with a lower consumption of power.
 It is difficult to select an optimum
  speed, however, because of the variation in shell
  diameter.
Hardinge Ball Mill
 Ball or tube mill operate
                   effectively only below its critical
Planetary mill     speed
                  Planetary mill obviate this
                   constraint by rotating the mill
                   simultaneously about its own axis
                   and about an axis of gyration.
                  In practice, several cylinders are
                   incorporated in the machine, all
                   rotating about the same axis of
                   gyration.
Planetary Ball Mill

 Smaller than common ball mills
 Mainly used in laboratories for grinding sample material
  down to very small sizes.
 Consist of at least one grinding jar which is arranged
  eccentrically on a so-called sun wheel.
 The difference in speeds between the balls and grinding
  jars produces an interaction between frictional and
  impact forces, which releases high dynamic energies.
 The interplay between these forces produces the high and
  very effective degree of size reduction of the planetary
  ball mill.
Vibration Mill

 By imparting a vibrating motion to a mill
      either by the rotation of out-of-balance weights or
      by the use of electro-mechanical devices,

 accelerations many times the gravitational
  acceleration may be imparted to the machine.
 The body of the machine is generally supported on
  powerful springs and caused to vibrate in a vertical
  direction.
 Grinding may take place in two stages, the material
  falling from an upper to a lower chamber when its
  size has been reduced below a certain value.
Vibration Mill

 Has much higher capacity than a conventional mill
  of the same size
 So either smaller equipment may be used or a much
  greater throughput is obtained.
 Well suited for incorporation in continuous grinding
  systems.
Vibration Mill
Colloid Mill

 Colloidal suspensions, emulsions and solid
  dispersions are produced by means of colloid mills or
  dispersion mills.
 Droplets or particles of sizes less than 1 μm may be
  formed
 Feed material of approximately 100-mesh or 50 μm
  in size is used
Rotor and stator of a Colloid Mill
Colloid Mill

 Clearances could be from virtually zero to 1.25
  mm, although in practice the maximum clearance used is
  about 0.3 mm
 The gap setting between rotor and stator is not
  necessarily in direct proportion to the droplet size or
  particle size of the end product.
 The thin film of material continually passing between the
  working surfaces is subjected to a high degree of
  shear, and consequently the energy absorbed within this
  film is frequently sufficient to reduce the dispersed phase
  to a particle size far smaller than the gap setting used.
Colloid Mill

 The rotor speed varies with the physical size of the
  mill and the clearance necessary to achieve the
  desired result
 The required operating conditions and size of mill
  can only be found by experiment.
 In all colloid mills, the power consumption is very
  high, and the material should therefore be ground as
  finely as possible before it is fed to the mill.
Fluid energy mill




http://www.sturtevantinc.com/demo/Micr
onizer.html
Fluid energy mill
Fluid energy mill

 solid is pulverised in jets of high pressure superheated
    steam or compressed air, supplied up to 3.5 MN/m2 (35
    bar).
   The pulverising takes place in a shallow cylindrical
    chamber with a number of jets arranged tangentially at
    equal intervals around the circumference.
   The solid is thrown to the outside walls of the chamber
   Fine particles are formed by the shearing action resulting
    from the differential velocities within the fluid streams.
   The jet pulveriser will give a product with a particle size
    of 1–10 μm.
Specialised applications

 Electrohydraulic crushing
      an underwater discharge is generated by the release of
       energy from a high-voltage capacitor
      The spark length depends on the nature of the material to be
       crushed
 Ultrasonic grinding
        fed between a drive roll and a curved plate, both of which are
         ultrasonically activated.
Specialised grinding--Cryogenic grinding

 Materials like plastics, rubber, waxes etc. tend to distort
    rather than to fracture when subjected to compressive
    forces.
   However can be done by subjecting it to very low
    temperatures.
   Material is cooled with liquid nitrogen at a temperature of
    about −196◦C (77K) to render it brittle before it enters the
    grinder
   cooling causes the crystal lattice to shrink and to give rise to
    microscopic cracks which act as nuclei and then grow
   thereby reducing the energy input required to cause
    fracturing to occur.
   Application in market for frozen foods
Specialised grinding--- Explosive Shattering

 energy is transmitted to particles as shock waves
 suddenly releasing steam from an explosion chamber
  containing the solid to be compressed.
 still at the development stage.

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Machinery for crushing and grinding

  • 1. Machinery for Crushing and Grinding
  • 2. Stag Jaw Crusher  The Stag jaw crusher has a fixed jaw and a moving jaw pivoted at the top  Crushing faces are formed of manganese steel.  The max movement of the jaw is at the bottom; so there is little tendency for the machine to clog, though some uncrushed material may fall through and have to be returned to the crusher.  The maximum pressure is exerted on the large material which is introduced at the top.  One of the toggle plates in the driving mechanism is made relatively weak so that, if any large stresses are set up, this is the first part to fail.  Easy renewal of the damaged part is then possible.
  • 5. Stag Jaw Crusher  The speed of operation should not be so high that a large quantity of fines is produced  The angle of nip, the angle between the jaws, is usually  about 30◦.  Because the crushing action is intermittent, the loading on the machine is uneven and the crusher therefore incorporates a heavy flywheel.  The power requirements of the crusher depend upon size and capacity and vary from 7 to about 70 kW,  the latter figure corresponding to a feed rate of 10 kg/s.
  • 6. Dodge Jaw Crusher  The moving jaw is pivoted at the bottom.  The minimum movement is thus at the bottom and a more uniform product is obtained  Although the crusher is less widely used because of its tendency to choke.  The large opening at the top enables it to take very large feed and to effect a large size reduction.  This crusher is usually made in smaller sizes than the Stag crusher, because of the high fluctuating stresses that are produced in the members of the machine.
  • 8. Dodge Jaw Crusher Both Crushers employs a compressive force for size reduction
  • 10. Gyratory Crusher  Crushing head is in the form of a truncated cone, mounted on a shaft  The crushing action takes place round the whole of the cone  The crusher is continuous in action, thus fluctuations in the stresses are smaller than in jaw crushers and the power consumption is lower.  It also does not take such a large size of feed as a jaw crusher, although it gives a rather finer and more uniform product.  Because the capital cost is high, the crusher is suitable only where large quantities of material are to be handled.  Employs a compressive force for size reduction
  • 11. Other Coarse Crushers – Coal Breaker  Consists of a large hollow cylinder with perforated walls.  Feed is introduced at the top.  The cylinder is rotated and the coal is lifted by means of arms attached to the inner surface and then falls against the cylindrical surface.  The coal breaks by impact and passes through the perforations as soon as the size has been sufficiently reduced.  This type of equipment is less expensive and has a higher throughput than the jaw or gyratory crusher.
  • 16. Edge Runner Mill  It has heavy cast iron or granite wheel, or muller mounted on a horizontal shaft which is rotated in a horizontal plane in a heavy pan.  Alternatively, the muller remains stationary and the pan is rotated  Material is fed to the centre of the pan and is worked outwards by the action of the muller, whilst a scraper continuously removes material that has adhered to the sides of the pan, and returns it to the crushing zone.
  • 17. Edge Runner Mill  In many models the outer rim of the bottom of the pan is perforated, so that the product may be removed continuously as soon as its size has been sufficiently reduced.  The mill may be operated wet or dry and it is used extensively for the grinding of paints, clays and sticky materials.
  • 19. Hammer Mill  Type of Impact mill with high speed rotating disc, to which are fixed a number of hammers  Hammers are swung outwards by centrifugal force.  Material is fed in, either at the top or at the centre, and it is thrown out centrifugally and crushed by hammer bars, or against breaker plates fixed around the periphery of the cylindrical casing.  The material is beaten until it is small enough to fall through the screen at the lower portion of the casing.  Hinged hammers: the presence of any hard material does not damage to equipment.
  • 20. Hammer Mill  The bars are replaced when they are worn out.  Suitable for the crushing of both brittle and fibrous materials  For fibrous materials it employs a screen with cutting edges.  Suitable for hard materials  Since a large amount of fines is produced, pressure lubrication is recommended for bearings.
  • 21. Hammer Mill  The size of the product is regulated by the size of the screen and the speed of rotation.  In some cases the hammer bars are rigidly fixed in position.  Since a large current of air is produced, the dust must be separated in a cyclone separator or a bag filter.
  • 24. Pin-type Mill  Two vertical steel plates  Horizontal projections at their near faces  One disc may be stationary whilst the other disc is rotated at high speed;  or the two may be rotated in opposite directions  The material is gravity fed in through a hopper or air and is thrown outwards by centrifugal action and  broken against of the projections before it is discharged to the outer body of the mill
  • 25. Pin type Mill  Discharged material falls under gravity  The mill gives a fairly uniform fine product with little dust  Used with chemicals, fertilisers and other materials that are non-abrasive, brittle or crystalline.  Control of the size of the product is effected by means of the speed and the spacing of the projections  and a product size of 20 μm is readily attainable.
  • 27. Single Roll Crusher  Consists of a toothed crushing roll  Roll rotates close to a breaker plate.  The material is crushed by compression and shearing between the two surfaces.  It is used extensively for crushing coal.
  • 30. Crushing Rolls  Two rolls, one in adjustable bearings, rotate in opposite directions  The clearance between them can be adjusted according to the size of feed and the required size of product.  Protected, by spring loading, against damage from very hard material.  Both rolls may be driven, or one directly and the other by friction with the solids.  Effect a small size reduction ratio, 4 : 1 in a single operation  commonly a no. of pairs of rolls are employed in series  one above the other
  • 31. Crushing Rolls  Roll shells with either smooth or ridged surfaces are held in place  See Ex. 2.2
  • 33. Symons Disc Crusher  Has 2 saucer-shaped discs mounted on horizontal shafts of which one is rotated  The two crushing faces continuously approach and recede.  Material is fed in the centre between the two discs  The product is discharged by centrifugal action as soon as it is fine enough to escape through the opening between the faces.
  • 36. Buhrstone mill  Grinding takes place between two heavy horizontal wheels, one of which is stationary and the other is driven.  The surface of the stones is carefully dressed so that the material is continuously worked outwards from the centre of the circumference of the wheels.  Size reduction takes place by a shearing action between the edges of the grooves on the two grinding stones.  Used for the grinding of grain, pigments, harmaceuticals, cosmetics and printer’s ink,  Although used where the quantity of material is very small.
  • 37. Roller Mill  The roller mill consists of a pair of rollers that rotate at different speeds in opposite directions.  one of the rollers is held in a fixed bearing whereas the other has an adjustable spring-loaded bearing  since the rollers rotate at different speeds, size reduction is effected by a combination of compressive and shear forces.  The roller mill is extensively used in the flour milling industry and for the manufacture of pigments for paints.
  • 39. Centrifugal Attrition Mills  Babcock Mill  The Lopulco mill or ring-roll pulveriser.  The NEI pendulum mill.
  • 41. Szego grinding mill  A planetary ring-roller mill  stationary, cylindrical grinding surface with a no. of grooved rollers rotate.  Connected to the central drive shaft; they are pushed outward by centrifugal force and roll on the grinding surface.  The material is fed by gravity is discharged at the bottom of the mill.
  • 42. Szego grinding mill  The particles, upon entering the grinding section, are repeatedly  crushed between the rollers and the stationary grinding surface.  Crushing and shearing force caused by rotational motion of the rollers.
  • 43. Ball Mill  Consists of a rotating hollow cylinder, partially filled with balls  Horizontal or at a small angle to the horizontal.  The outlet is normally covered with a coarse screen to prevent the escape of the balls  Balls fall on the grinding medium from a height  Size reduction mainly by Impact, Compression and Attrition
  • 45. Ball Mill  Inner surface of the cylinder is lined with an abrasion- resistant material  such as manganese steel, stoneware or rubber.  Balls occupy a volume b/n 30 and 50 per cent of total volume of the mill  Balls wear out during grinding and are replaced  Different sized balls may be used  large balls deal effectively with the feed and the small ones are responsible for giving a fine product.  For very fine grinding in small mills pebbles are often used instead of balls.
  • 46. Compound Ball Mill  Cylinder is divided into compartments by vertical perforated plates.  Material flows axially along the mill  Can pass from one compartment to the next only when its size has been reduced to less than the perforations in the plate.  Each compartment is supplied with balls of a different size.  large balls are at the entry while the small balls before discharge.  Results in economical operation and the formation of a uniform product.
  • 47. Wet grinding in Ball Mill  Power consumption is generally about 30 per cent lower than that for dry grinding  Continuous removal of product as it is formed is facilitated
  • 48. Factors affecting the size of the product  The rate of feed.  With high rates of feed, less size reduction is effected  The properties of the feed material.  The larger the feed the larger is the product  A smaller size reduction is obtained with a hard material.  Weight of balls.  A heavy charge of balls produces a fine product.  The weight of the charge can be increased, either by increasing the number of balls, or by using a material of higher density
  • 49. Factors affecting the size of the product  Diameter of the balls.  Small balls facilitate the production of fine material  But do not deal so effectively with the larger particles in the feed. The  For an economical operation, the smallest possible balls should be used.  The slope of the mill.  An increase in the slope of the mill increases the capacity  But a coarser product is obtained.  Discharge freedom.  same effect as increasing the slope.
  • 50. Factors affecting the size of the product  The speed of rotation of the mill– Critical Speed  Low speeds of rotation, the balls simply roll over one another and little crushing  At still higher speeds they are thrown greater distances  At very high speeds, the balls are carried right round in contact with the sides of the mill and little relative movement or grinding takes place again.  The minimum speed at which the balls are carried round in this manner is called the critical speed of the mill  Hence at Critical speed there will be no resultant force acting on the ball when in the uppermost position
  • 51. Factors affecting the size of the product  At critical speed the centrifugal force will be exactly equal to the weight of the ball.  If the mill is rotating at the critical angular velocity ω  rω2 = g  Nc is the no. of revolutions per unit time  It is found that the optimum speed is between one- half and three-quarters of the critical speed.
  • 52. Ball mill at correct Critical speed
  • 53. Factors affecting the size of the product  The level of material in the mill.  Power consumption is reduced by maintaining a low level of material  can be done by providing suitable discharge opening for the product.  If the level of material is raised, the cushioning action is increased and power is wasted by the production of an excessive quantity of undersize material.
  • 54. Advantages of the Ball Mill  The mill may be used wet or dry  The costs of installation and power are low.  The ball mill may be used with an inert atmosphere and therefore can be used for the grinding of explosive materials.  The grinding medium is cheap.  The mill is suitable for materials of all degrees of hardness.  It may be used for batch or continuous operation.  It may be used for open or closed circuit grinding.
  • 55. Tube Mill  Similar to ball mill  However, length to the diameter is usually 3 or 4 : 1, as compared with 1 or 1.5 : 1 for the ball mill.  The mill is filled with pebbles  The characteristics of the two mills are similar  But material remains longer in the tube mill because of its greater length, and a finer product is therefore obtained.
  • 56. Rod Mill  High carbon steel rods about 50 mm diameter and extending the whole length of the mill are used.  This mill gives a very uniform fine product  Power consumption is low  Not suitable for very tough materials and  Feed should not exceed about 25 mm in size.  It is particularly useful with sticky materials which would hold the balls together in aggregates, because the greater weight  of the rods causes them to pull apart again.  Worn rods must be removed from time to time and replaced by new ones, which are rather cheaper than balls.
  • 57. Hardinge Mill  A ball mill in which the balls segregate themselves according to size.  The main portion of the mill is cylindrical as in the ball mill, although the outlet end is conical and tapers towards the discharge point  large balls collect in the cylindrical portion while the smaller balls, in order of decreasing size,  Like a Compound Ball Mill
  • 59. Hardinge Mill  The mill has an advantage over the compound ball mill in that the large balls are raised to the greatest height and therefore are able to exert the maximum force on the feed.  As the size of the material is reduced, smaller forces are needed to cause fracture and it is therefore unnecessary to raise the smaller balls as high.  The capacity of the Hardinge mill is higher than that of a ball mill of similar size and it gives a finer and more uniform product with a lower consumption of power.  It is difficult to select an optimum speed, however, because of the variation in shell diameter.
  • 61.  Ball or tube mill operate effectively only below its critical Planetary mill speed  Planetary mill obviate this constraint by rotating the mill simultaneously about its own axis and about an axis of gyration.  In practice, several cylinders are incorporated in the machine, all rotating about the same axis of gyration.
  • 62. Planetary Ball Mill  Smaller than common ball mills  Mainly used in laboratories for grinding sample material down to very small sizes.  Consist of at least one grinding jar which is arranged eccentrically on a so-called sun wheel.  The difference in speeds between the balls and grinding jars produces an interaction between frictional and impact forces, which releases high dynamic energies.  The interplay between these forces produces the high and very effective degree of size reduction of the planetary ball mill.
  • 63. Vibration Mill  By imparting a vibrating motion to a mill  either by the rotation of out-of-balance weights or  by the use of electro-mechanical devices,  accelerations many times the gravitational acceleration may be imparted to the machine.  The body of the machine is generally supported on powerful springs and caused to vibrate in a vertical direction.  Grinding may take place in two stages, the material falling from an upper to a lower chamber when its size has been reduced below a certain value.
  • 64. Vibration Mill  Has much higher capacity than a conventional mill of the same size  So either smaller equipment may be used or a much greater throughput is obtained.  Well suited for incorporation in continuous grinding systems.
  • 66. Colloid Mill  Colloidal suspensions, emulsions and solid dispersions are produced by means of colloid mills or dispersion mills.  Droplets or particles of sizes less than 1 μm may be formed  Feed material of approximately 100-mesh or 50 μm in size is used
  • 67. Rotor and stator of a Colloid Mill
  • 68. Colloid Mill  Clearances could be from virtually zero to 1.25 mm, although in practice the maximum clearance used is about 0.3 mm  The gap setting between rotor and stator is not necessarily in direct proportion to the droplet size or particle size of the end product.  The thin film of material continually passing between the working surfaces is subjected to a high degree of shear, and consequently the energy absorbed within this film is frequently sufficient to reduce the dispersed phase to a particle size far smaller than the gap setting used.
  • 69. Colloid Mill  The rotor speed varies with the physical size of the mill and the clearance necessary to achieve the desired result  The required operating conditions and size of mill can only be found by experiment.  In all colloid mills, the power consumption is very high, and the material should therefore be ground as finely as possible before it is fed to the mill.
  • 72. Fluid energy mill  solid is pulverised in jets of high pressure superheated steam or compressed air, supplied up to 3.5 MN/m2 (35 bar).  The pulverising takes place in a shallow cylindrical chamber with a number of jets arranged tangentially at equal intervals around the circumference.  The solid is thrown to the outside walls of the chamber  Fine particles are formed by the shearing action resulting from the differential velocities within the fluid streams.  The jet pulveriser will give a product with a particle size of 1–10 μm.
  • 73. Specialised applications  Electrohydraulic crushing  an underwater discharge is generated by the release of energy from a high-voltage capacitor  The spark length depends on the nature of the material to be crushed  Ultrasonic grinding  fed between a drive roll and a curved plate, both of which are ultrasonically activated.
  • 74. Specialised grinding--Cryogenic grinding  Materials like plastics, rubber, waxes etc. tend to distort rather than to fracture when subjected to compressive forces.  However can be done by subjecting it to very low temperatures.  Material is cooled with liquid nitrogen at a temperature of about −196◦C (77K) to render it brittle before it enters the grinder  cooling causes the crystal lattice to shrink and to give rise to microscopic cracks which act as nuclei and then grow  thereby reducing the energy input required to cause fracturing to occur.  Application in market for frozen foods
  • 75. Specialised grinding--- Explosive Shattering  energy is transmitted to particles as shock waves  suddenly releasing steam from an explosion chamber containing the solid to be compressed.  still at the development stage.