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PHARMACUTICAL UNIT OPEARTION:
SIZE REDUCTION
Pravin B. Awate ( M. Pharm Pharmaceutics)
Assistant Professor
RDCOP, BHOR
Size Reduction
Content…
 Objectives,
 Mechanisms & Laws governing size reduction,
factors affecting size reduction,
 Principles, construction, working, uses, merits and demerits of
Hammer mill, ball mill, fluid energy mill, Edge runner mill & end runner
mill.
Size Reduction
INTRODUCTION:
 Size reduction or comminution is the process of reducing drugs
(vegetable and chemical substances) into smaller pieces, coarse particles or
fine powder.
 Size reduction is the operation carried out for reducing the size of
bigger particles into smaller one of desired size and shape with the help of
external forces.
 COMMINUTION is another term used for size reduction.
 Size refers to physical Dimension of an object, whereas Reduction
refers to decrement or the process of decreasing the size.
Size reduction process is also termed as comminution or diminution 'or
pulverisation.
 Normally, size reduction may be achieved by two methods, namely
precipitation or mechanical process.
Size reduction may be achieved by two methods:
1] Precipitation
2] Mechanical process
 In the precipitation method, the substance is dissolved in an appropriate solvent.
Subsequently, it is finely precipitated by the addition of another solvent, which is
miscible with the first, but in the later the substance isinsolu.ble; This method is
suitable for the production of raw materials and bulk drugs.
 Inorganic chemicals, such as calcium carbonate, magnesium carbonate and· yellow
mercuric oxide, are prepared by precipitation Method.
 In the mechanical process, the substance is subjected to mechanical forces using
grincling equipment (ball mill, roller mill, colloid mill etc.). In general, dry grinding or
milling is used in the production of tablets and capsules, while wet grinding is used in
the preparation of suspensions, emulsions and ointments.
The method of milling is applied either in the production of raw materials or as a
part of the production cycle ·in the manufacture of dosage forms.
Pharmaceutical Applications/ Importance of Particle Size Reduction
The process of size reduction is commonly employed in pharmaceutical
industries due to the following reasons:
1. To increase the rate of solution in case of chemical substances, because
reduction of the particle size increases the surface area for the action of
solvent.
2. To allow the rapid penetration of the solvent (menstrum), in case of crude
drugs for the extraction of active constituents from vegetable and animal
drugs.
3. To get a uniform powder because particle size reduction helps in uniform
mixing of drugs, required for preparing different formulations for
administration.
4. To increase the rate of absorption of a drug. The smaller the particle
size, the greater is the rate of absorption.
5. To improve the stability of certain pharmaceutical dosage form, such as
suspensions. The rate of sedimentation decreases to a large extent by
reducing the particle size of the drug.
6. To help in the process of separation of solids from liquids by filtration
or by sedimentation. The rate of filtration or sedimentation depends upon
the particle size.
ADVANTAGES OF SIZE REDUCTION
1. Content uniformity:
Mixing of different ingredients can be effective, if the particle size is uniform and
small. Particles of optimum size are desirable for effective mixing.
2. Uniform flow:
Smaller particle size! and controlled size distribution, promote the flow of the. powder
into dies during compression of tablets The same principles are used in the production
of capsules.
3. Effective extraction of drugs:
Smaller particles allow rapid penetration of menstruum or solvent into the tissue or
cells of vegetable and animal origin (liver and pancreas). As a result, extraction or
leaching of active constituent; becomes effective and complete in preparation of
galenicals. The time required for extraction can be shortened.
4. Effective drying:
Drying of a granular mass can be·rapid and effective, if the size of granules is small
and uniform .
5. Improved physical stability:
In case of suspensions and emulsions, the rate of sedimentation decreases to a large
extent if particle size is small.
6. Improved dissolution rate :
Size reduction increases surface area, which facilitates intimate contact of solid
particles and gastric or intestinal juices. Thus, the rate of dissolution enhances.
7. Improved rate of absorption : The smaller the particle size, the faster is the
absorption, because of enhanced dissolution.
DISADVANTAGES
1.Drug degradation:
Drug decomposition is possible due to the heat produced,· during milling.
Thermo-labile substances are the most affected. The increased surface
area also facilitates drug decomposition owing to enhanced dissolution.
Cooling support systems are provided to decrease the heat in milling
equipment. Drugs containing waxy materials become soft due to heat
generated during milling. Therefore the feed is chilled before milling.
2. Poor mixing :
Normally, very small particles possess strong cohesive forces, hence,
aggregation of particles is possible. Aggregation inhibits the effective
blending of different additives.
An increase in surface area may promote the adsorption of air, which may
inhibit wettability of the drug during production. Therefore, optimum·
particle size is desirable to improve blending and to avoid poor mixing.
3. Contamination :
During milling and grinding. the grinding surfaces wear off (examples are
ceramic or iron equipment), the particles of which are present as impurities
in the powder. Such type of mills should be avoided, when drugs of high
purity are required.
.
Factors Affecting Size Reduction
The following factors affect the process of size reduction:
1. Hardness :
The hardness of the material affects the process of size reduction. It is easier to
break soft material to a small size than hard material.
2. Toughness :
The crude drugs of fibrous nature or those having higher moisture content, are
generally tough in nature.
A soft but tough material may present more problem in size reduction, than a hard
but brittle substance.
3. Stickiness :
Stickiness causes a lot of difficulty in size reduction. This is due to the fact that
material adheres to the grinding surfaces or sieve surface of the mill. It
difficult to powder a drugs of having gummy or resinous nature, if the method used
for size reduction generates heat. Complete dryness of material may help to
overcome this difficulty.
4. Material structure :
Materials which show some special structure may cause problem during size
reduction e.g. vegetable drugs which have cellular structure, generally produce long
fibrous particles on its size reduction. Similarly a mineral substance having lines of
weakness, produces flake like particles on its size reduction.
Factors Affecting Size Reduction
5. Moisture content :
The presence of moisture in the material influences a number of its properties such as
hardness, toughness or stickiness which in its turn affects the particle size reduction.
The material should be either dry or wet. It should not be damp. The material having
5% moisture in case of dry grinding and 50% moisture in wet grinding does not
create any problem.
6. Softening temperature :
Waxy substances such as stearic acid or drugs containing oils or fats, become softened
during the size reduction processes, if heat is generated. This can be avoided by
cooling the mill.
7. Purity required :
Various mills used for size reduction often cause the grinding surfaces to wear off and
thus impurities come in the powder. If a high degree of purity is required, such mills
must be avoided. Moreover, the mills should be thoroughly cleansed between batches of
different materials in order to maintain purity.
8.Physiological effect :
Some drugs are very potent. During their particle size reduction in a mill, dust is
produced which may have an effect on the operator. In such cases, the enclosed mills
may be used to avoid dust.
9. Ratio of feed size to product size : To get a fine powder in a mill it is required
that a fairly small feed size should be used. Hence it is necessary to carry out the size
reduction process in several stages, using different equipment e.g. preliminary
crushing followed by coarse powder and then fine grinding.
10. Bulk density : The output of the size reduction of material in a machine, depends
upon the bulk density of the substance.
METHODS OF SIZE REDUCTION
The following are the methods of size reduction, in which different mechanisms are
involved:
1. Cutting The material is cut on a small scale by means of a sharp blade, knife root
cutter or any other sharp instrument. On a large scale, a cutter mill is used. Cutting of
drug is usually done to hasten the drying of drugs.
2. Compression: In this method, the material is crushed by the application of pressure.
On a small scale, size reduction is carried out by using pestle and mortar, whereas on a
large scale, roller mill is used.
3. Impact: It occurs when the material is more or less stationary and is hit by an
object moving at high speed or when the moving particle strikes a stationary surface. In
either case, the material breaks into small pieces. There is no apparatus which can be
used on a small scale to affect size reduction by impact. But on a large scale, hammer
mill and disintegrator are used when size reduction of material is done by impact.
4. Attrition
This process involves breaking down of the material by rubbing action between two
surfaces, i.e., surface phenomena. Example is fluid energy ·mill
5. Combined impact and attrition
CLASS!FICATION OF SIZE REDUCTION EQUIPMENT
HAMMER MILL
Principle .:
The hammer mill operates on the
principle· of impact between. rapidly
moving hammers mounted on a rotor and·
the powder material.
Construction:
It consists of a stout metal casing,
enclosing a central shaft, to which four
or more swinging hammers are attached.
The lower part of the casing consists of
a screen, through which material can
pass and collected in a suitable receiver,
when the desired degree of size
reduction is reached.
Working :
The material is put into the hopper which
is connected with the drum. These
rotating hammers beat the material to
yield smaller particles The material is
powdered to the desired size, due to
fast rotation of hammers and is collected
under the screen.
HAMMER MILL
Uses:
Particle size obtained from 10-400mm.
Also used to mill dry, wet and filter press cakes materials.
Advantage:
It is rapid in action, and is capable of grinding many different types of materials.
They are easy to install and operate, the operation is continuous.
There is little contamination of the product with metal abraded from the mill as no
surface move against each other.
The particle size of the material to be reduced can be easily controlled by changing the
speed of the rotor, hammer type, shape and size of the screen.
 Operated in a closed environment dust can. be reduced and explosion hazards can be
prevented.
Disadvantage:
 Heat build-up during milling is more, therefore, product degradation is possible.
 Hammer mills cannot be employed to mill sticky, fibrous and hard materials.
The screens may get clogged.
Wearing of mill and screen is more with abrasive materials.
BALL MILL
These are also known as tumbling mills or
pebble mills.
Principle:
The ball mill works on the principle of impact
between rapidly moving balls
and the powder material enclosed in a hollow
cylinder.
At low speed the balls roll over each other
attrition will be mode of action thus in the
ball mill attrition and impact both
mechanisms takes place.
Construction:
 It consists of a hollow cylinder which is
mounted on a metallic frame in such a way
that it can be rotated on its longitudinal axis.
 The length of the cylinder is slightly
higher than its diameter.
 The cylinder contains balls that occupy 30
to 50% of the mill volume.
 The ball size depends on the size of the
feed and the diameter of the mill.
 Balls are made up of steel, iron or
stoneware and act as grinding medium.
BALLMILL
The drug to be ground is put into the cylinder of
the mill and is rotated. The speed of rotation is
very important.
 At a low speed, the mass of balls will slide or roll
over each other and only a negligible amount of size
reduction will occur.
 At a high speed, the balls will be thrown out to
the walls by centrifugal force and no grinding will
occur.
The compression by the balls against the wall will
not be sufficient for (effective comminution of the
substance.
 At correct speed, the centrifugal force just
occurs, as a result the balls are picked up by the
mill wall and carried nearly to the top, where they
break contact with the wall and fall to the bottom
to be picked up.
In this manner, impact stress will also be induced
and the size reduction is made effective.
 Advantages
It can produce very fine powder. Ball mill is used
for both wet and dry grinding processes.
Toxic substances can be ground, as the cylinder is
closed system. Rod or bars can also be used as
grinding media. (example: Sticky material are size
reduced)
In ball mill, installation, operation and labour costs
are low.
Disadvantages
The ball mill is a very noisy machine.
Ball mill is a slow process. Soft, tacky,
fibrous material cannot be milled by ball mill.
Uses:
 For fine grinding with a particle size of
100 to 5 mm or less.
 For production of ophthalmic and parenteral
products.
 For milling dyes, pigments and insecticides
at low speed
FLUID ENERGY MILL
Principle:
Fluid energy mill operates on the principle
of impact and attrition. Milling takes
place because of high velocity collisions
between the suspended particles.
Construction:
It consist of an elliptical pipe which has a
height of about 2 meters and diameter
may be ranging from 20 to 200 mm. The
mill surface may be made up of either
soft stainless steel or tough ceramics.
Grinding nozzles are placed tangential and
opposed to the initial flow path of a
powder. Compressed air is used at 600
kilopascals to 1 megapascals. Venturi
feeder is provided in the path of the
airflow. An outlet with a classifier is
fitted to allow the escape of air.
FLUID ENERGY MILL
Working:
The air or inert gas is introduced with a very
high pressure through the nozzles. Solids are
introduced into air stream through inlet. Due
to high degree of turbulence, impact and
attritional forces occurs between the
particles. The fine particles are collected
through a classifier. Fluid energy mill reduces
the particles to 1 to 20 micron To get a very
fine powder, even up to five micron, the
material is pre-treated to reduce the
particle size to the order of 100 mesh and
then passed through fluid energy mill.
Uses
The mill is used to grind heat sensitive
material to tine powder. The mill is used to
grind those drugs in which high degree of
purity is required.
Advantages of Fluid Energy Mill
1. The mill is used to grind the material
to fine powder.
2. The particle size of powder can be
controlled due to the use of a classifier.
3. There is no wear of the mill and
hence there is no contamination of the
product.
4. It is useful for grinding heat
sensitive substances such as
sulphonamides, vitamins and antibiotics
EDGE RUNNER MILL
Principle:
The size reduction is done by crushing
(Compression) due to heavy weight of stones
and shearing force which is involved during
the movement of these stones.
Construction
It consists of two heavy rollers and a. bed
made of stone or granite. The rollers have a
central shaft and they revolve on its axis.
The rollers are mounted on a horizontal shaft
and move around the bed.
Working:
The material to be ground is put on the bed
and with the help of the scrapers 'it is kept
in the path of the stone wheels. The material
is ground for a definite period and then it is
passed through the sieves to get powder of
the required size.
Uses:
Edge runner mill is used for grinding most of
tough drugs to fine powder.
Disadvantages:
Occupies more space
Contamination of product with roller
is possible
Time consuming process
Not employed for sticky materials
Energy consumption is high.
EDGE RUNNER MILL
END RUNNER MILL
Principle:
Size reduction is done by crushing
(compression) due to heavy weight of steel
pestle. Shearing stress is also involved
during the movement of mortar and pestle.
Construction:
It is considered as mechanical mortar and
pestle. It consist of steel mortar which is
fixed to Flanged plate. Underneath the
flanged plate, a bevelled cog fitting is
attached to horizontal shaft bearing a pulley.
Hence the plate and mortar can be rotated
with the high speed.
The pestle is dumb bell shaped so that
balancing and efficient grinding by its weight
can be achieved. The bottom of pestle is flat
rather than round. The pestle carries an arm
which is hinged. By this arrangement, the
pestle can be raised from mortar to
facilitate emptying and cleaning. The narrow
central portion of pestle is longer than the
band around it. Hence pestle can rise and fall
over material in the mortar.
Working : The. Material to be
ground placed in mortar .The
scrapper puts the material in the
path of pestle. The mortar revolves
at a high speed . The pestle is placed
in the mortar. The revolving mortar
causes pestle to move. During this
process, size reduction is being
achieved by Shearing as well as
crushing. The material is being
collected and passed through a sieve
to get a the powder of desired size.
Use:
It is suitable for fine grinding.
Disadvantages:
Not suitable for unbroken or slightly
broken condition of drug.
END RUNNER MILL
. .
THEORIES OF SIZE REDUCTION / MILLING
A number of theories have been proposed to establish a
relationship between energy input and the degree of size
reduction produced.
1. Rittinger’s theory
2. Bond’s theory
3. Kick’s theory
4. Walker’s theory
RITTINGER’S THEORY
Rittinger’s theory suggests that energy required in a size reduction
process is proportional to the new surface area produced.
where,
E = energy required for size reduction
KR = Rittinger’s constant
Si = initial specific surface area
Sn = final specific surface area
Application:
It is most applicable in size reducing brittle materials undergoing
fine milling.
BOND’S THEORY
Bond’s theory states that the energy used in crack propagation is
proportional to the new crack length produced.
where,
E = energy required for size reduction
KB = Bond’s work index
di = initial diameter of particles
dn = final diameter of particles
Application:
This law is useful in rough mill sizing. The work index is useful in
comparing the efficiency of milling operations.
KICK’S THEORY
Kick’s theory states that the energy used in deforming (or
fracturing) a set of particles of equivalent shape is proportional to
the ratio of change of size, or:
where, E = energy required for size reduction
KK = Kick’s constant
di = initial diameter of particles
dn = final diameter of particles
Application:
For crushing of large particles Kick’s theory most useful.
WALKER’S THEORY
Walker proposed a generalized differential form of the energy-
size relationship:
where
E = amount of energy (work done) required to produce a change
D = size of unit mass
K = Constant
n = constant
For n =1.0 Walker equation becomes Kick’s theory used for coarse
particles > 1 m.
For n =1.5 Walker equation becomes Bond’s theory. This theory is
used when neither Kick’s nor Rittinger’s law is applicable.
For n =2.0 Walker equation becomes Rittinger’s theory used for
fine particles < 1 m size.
Size reduction

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Size reduction

  • 1. PHARMACUTICAL UNIT OPEARTION: SIZE REDUCTION Pravin B. Awate ( M. Pharm Pharmaceutics) Assistant Professor RDCOP, BHOR
  • 2. Size Reduction Content…  Objectives,  Mechanisms & Laws governing size reduction, factors affecting size reduction,  Principles, construction, working, uses, merits and demerits of Hammer mill, ball mill, fluid energy mill, Edge runner mill & end runner mill.
  • 3. Size Reduction INTRODUCTION:  Size reduction or comminution is the process of reducing drugs (vegetable and chemical substances) into smaller pieces, coarse particles or fine powder.  Size reduction is the operation carried out for reducing the size of bigger particles into smaller one of desired size and shape with the help of external forces.  COMMINUTION is another term used for size reduction.  Size refers to physical Dimension of an object, whereas Reduction refers to decrement or the process of decreasing the size. Size reduction process is also termed as comminution or diminution 'or pulverisation.  Normally, size reduction may be achieved by two methods, namely precipitation or mechanical process.
  • 4. Size reduction may be achieved by two methods: 1] Precipitation 2] Mechanical process  In the precipitation method, the substance is dissolved in an appropriate solvent. Subsequently, it is finely precipitated by the addition of another solvent, which is miscible with the first, but in the later the substance isinsolu.ble; This method is suitable for the production of raw materials and bulk drugs.  Inorganic chemicals, such as calcium carbonate, magnesium carbonate and· yellow mercuric oxide, are prepared by precipitation Method.  In the mechanical process, the substance is subjected to mechanical forces using grincling equipment (ball mill, roller mill, colloid mill etc.). In general, dry grinding or milling is used in the production of tablets and capsules, while wet grinding is used in the preparation of suspensions, emulsions and ointments. The method of milling is applied either in the production of raw materials or as a part of the production cycle ·in the manufacture of dosage forms.
  • 5. Pharmaceutical Applications/ Importance of Particle Size Reduction The process of size reduction is commonly employed in pharmaceutical industries due to the following reasons: 1. To increase the rate of solution in case of chemical substances, because reduction of the particle size increases the surface area for the action of solvent. 2. To allow the rapid penetration of the solvent (menstrum), in case of crude drugs for the extraction of active constituents from vegetable and animal drugs. 3. To get a uniform powder because particle size reduction helps in uniform mixing of drugs, required for preparing different formulations for administration. 4. To increase the rate of absorption of a drug. The smaller the particle size, the greater is the rate of absorption. 5. To improve the stability of certain pharmaceutical dosage form, such as suspensions. The rate of sedimentation decreases to a large extent by reducing the particle size of the drug. 6. To help in the process of separation of solids from liquids by filtration or by sedimentation. The rate of filtration or sedimentation depends upon the particle size.
  • 6. ADVANTAGES OF SIZE REDUCTION 1. Content uniformity: Mixing of different ingredients can be effective, if the particle size is uniform and small. Particles of optimum size are desirable for effective mixing. 2. Uniform flow: Smaller particle size! and controlled size distribution, promote the flow of the. powder into dies during compression of tablets The same principles are used in the production of capsules. 3. Effective extraction of drugs: Smaller particles allow rapid penetration of menstruum or solvent into the tissue or cells of vegetable and animal origin (liver and pancreas). As a result, extraction or leaching of active constituent; becomes effective and complete in preparation of galenicals. The time required for extraction can be shortened. 4. Effective drying: Drying of a granular mass can be·rapid and effective, if the size of granules is small and uniform . 5. Improved physical stability: In case of suspensions and emulsions, the rate of sedimentation decreases to a large extent if particle size is small. 6. Improved dissolution rate : Size reduction increases surface area, which facilitates intimate contact of solid particles and gastric or intestinal juices. Thus, the rate of dissolution enhances. 7. Improved rate of absorption : The smaller the particle size, the faster is the absorption, because of enhanced dissolution.
  • 7. DISADVANTAGES 1.Drug degradation: Drug decomposition is possible due to the heat produced,· during milling. Thermo-labile substances are the most affected. The increased surface area also facilitates drug decomposition owing to enhanced dissolution. Cooling support systems are provided to decrease the heat in milling equipment. Drugs containing waxy materials become soft due to heat generated during milling. Therefore the feed is chilled before milling. 2. Poor mixing : Normally, very small particles possess strong cohesive forces, hence, aggregation of particles is possible. Aggregation inhibits the effective blending of different additives. An increase in surface area may promote the adsorption of air, which may inhibit wettability of the drug during production. Therefore, optimum· particle size is desirable to improve blending and to avoid poor mixing. 3. Contamination : During milling and grinding. the grinding surfaces wear off (examples are ceramic or iron equipment), the particles of which are present as impurities in the powder. Such type of mills should be avoided, when drugs of high purity are required. .
  • 8. Factors Affecting Size Reduction The following factors affect the process of size reduction: 1. Hardness : The hardness of the material affects the process of size reduction. It is easier to break soft material to a small size than hard material. 2. Toughness : The crude drugs of fibrous nature or those having higher moisture content, are generally tough in nature. A soft but tough material may present more problem in size reduction, than a hard but brittle substance. 3. Stickiness : Stickiness causes a lot of difficulty in size reduction. This is due to the fact that material adheres to the grinding surfaces or sieve surface of the mill. It difficult to powder a drugs of having gummy or resinous nature, if the method used for size reduction generates heat. Complete dryness of material may help to overcome this difficulty. 4. Material structure : Materials which show some special structure may cause problem during size reduction e.g. vegetable drugs which have cellular structure, generally produce long fibrous particles on its size reduction. Similarly a mineral substance having lines of weakness, produces flake like particles on its size reduction.
  • 9. Factors Affecting Size Reduction 5. Moisture content : The presence of moisture in the material influences a number of its properties such as hardness, toughness or stickiness which in its turn affects the particle size reduction. The material should be either dry or wet. It should not be damp. The material having 5% moisture in case of dry grinding and 50% moisture in wet grinding does not create any problem. 6. Softening temperature : Waxy substances such as stearic acid or drugs containing oils or fats, become softened during the size reduction processes, if heat is generated. This can be avoided by cooling the mill. 7. Purity required : Various mills used for size reduction often cause the grinding surfaces to wear off and thus impurities come in the powder. If a high degree of purity is required, such mills must be avoided. Moreover, the mills should be thoroughly cleansed between batches of different materials in order to maintain purity. 8.Physiological effect : Some drugs are very potent. During their particle size reduction in a mill, dust is produced which may have an effect on the operator. In such cases, the enclosed mills may be used to avoid dust. 9. Ratio of feed size to product size : To get a fine powder in a mill it is required that a fairly small feed size should be used. Hence it is necessary to carry out the size reduction process in several stages, using different equipment e.g. preliminary crushing followed by coarse powder and then fine grinding. 10. Bulk density : The output of the size reduction of material in a machine, depends upon the bulk density of the substance.
  • 10. METHODS OF SIZE REDUCTION The following are the methods of size reduction, in which different mechanisms are involved: 1. Cutting The material is cut on a small scale by means of a sharp blade, knife root cutter or any other sharp instrument. On a large scale, a cutter mill is used. Cutting of drug is usually done to hasten the drying of drugs. 2. Compression: In this method, the material is crushed by the application of pressure. On a small scale, size reduction is carried out by using pestle and mortar, whereas on a large scale, roller mill is used. 3. Impact: It occurs when the material is more or less stationary and is hit by an object moving at high speed or when the moving particle strikes a stationary surface. In either case, the material breaks into small pieces. There is no apparatus which can be used on a small scale to affect size reduction by impact. But on a large scale, hammer mill and disintegrator are used when size reduction of material is done by impact. 4. Attrition This process involves breaking down of the material by rubbing action between two surfaces, i.e., surface phenomena. Example is fluid energy ·mill 5. Combined impact and attrition
  • 11. CLASS!FICATION OF SIZE REDUCTION EQUIPMENT
  • 12. HAMMER MILL Principle .: The hammer mill operates on the principle· of impact between. rapidly moving hammers mounted on a rotor and· the powder material. Construction: It consists of a stout metal casing, enclosing a central shaft, to which four or more swinging hammers are attached. The lower part of the casing consists of a screen, through which material can pass and collected in a suitable receiver, when the desired degree of size reduction is reached. Working : The material is put into the hopper which is connected with the drum. These rotating hammers beat the material to yield smaller particles The material is powdered to the desired size, due to fast rotation of hammers and is collected under the screen.
  • 13. HAMMER MILL Uses: Particle size obtained from 10-400mm. Also used to mill dry, wet and filter press cakes materials. Advantage: It is rapid in action, and is capable of grinding many different types of materials. They are easy to install and operate, the operation is continuous. There is little contamination of the product with metal abraded from the mill as no surface move against each other. The particle size of the material to be reduced can be easily controlled by changing the speed of the rotor, hammer type, shape and size of the screen.  Operated in a closed environment dust can. be reduced and explosion hazards can be prevented. Disadvantage:  Heat build-up during milling is more, therefore, product degradation is possible.  Hammer mills cannot be employed to mill sticky, fibrous and hard materials. The screens may get clogged. Wearing of mill and screen is more with abrasive materials.
  • 14. BALL MILL These are also known as tumbling mills or pebble mills. Principle: The ball mill works on the principle of impact between rapidly moving balls and the powder material enclosed in a hollow cylinder. At low speed the balls roll over each other attrition will be mode of action thus in the ball mill attrition and impact both mechanisms takes place. Construction:  It consists of a hollow cylinder which is mounted on a metallic frame in such a way that it can be rotated on its longitudinal axis.  The length of the cylinder is slightly higher than its diameter.  The cylinder contains balls that occupy 30 to 50% of the mill volume.  The ball size depends on the size of the feed and the diameter of the mill.  Balls are made up of steel, iron or stoneware and act as grinding medium.
  • 15. BALLMILL The drug to be ground is put into the cylinder of the mill and is rotated. The speed of rotation is very important.  At a low speed, the mass of balls will slide or roll over each other and only a negligible amount of size reduction will occur.  At a high speed, the balls will be thrown out to the walls by centrifugal force and no grinding will occur. The compression by the balls against the wall will not be sufficient for (effective comminution of the substance.  At correct speed, the centrifugal force just occurs, as a result the balls are picked up by the mill wall and carried nearly to the top, where they break contact with the wall and fall to the bottom to be picked up. In this manner, impact stress will also be induced and the size reduction is made effective.  Advantages It can produce very fine powder. Ball mill is used for both wet and dry grinding processes. Toxic substances can be ground, as the cylinder is closed system. Rod or bars can also be used as grinding media. (example: Sticky material are size reduced) In ball mill, installation, operation and labour costs are low. Disadvantages The ball mill is a very noisy machine. Ball mill is a slow process. Soft, tacky, fibrous material cannot be milled by ball mill. Uses:  For fine grinding with a particle size of 100 to 5 mm or less.  For production of ophthalmic and parenteral products.  For milling dyes, pigments and insecticides at low speed
  • 16. FLUID ENERGY MILL Principle: Fluid energy mill operates on the principle of impact and attrition. Milling takes place because of high velocity collisions between the suspended particles. Construction: It consist of an elliptical pipe which has a height of about 2 meters and diameter may be ranging from 20 to 200 mm. The mill surface may be made up of either soft stainless steel or tough ceramics. Grinding nozzles are placed tangential and opposed to the initial flow path of a powder. Compressed air is used at 600 kilopascals to 1 megapascals. Venturi feeder is provided in the path of the airflow. An outlet with a classifier is fitted to allow the escape of air.
  • 17. FLUID ENERGY MILL Working: The air or inert gas is introduced with a very high pressure through the nozzles. Solids are introduced into air stream through inlet. Due to high degree of turbulence, impact and attritional forces occurs between the particles. The fine particles are collected through a classifier. Fluid energy mill reduces the particles to 1 to 20 micron To get a very fine powder, even up to five micron, the material is pre-treated to reduce the particle size to the order of 100 mesh and then passed through fluid energy mill. Uses The mill is used to grind heat sensitive material to tine powder. The mill is used to grind those drugs in which high degree of purity is required. Advantages of Fluid Energy Mill 1. The mill is used to grind the material to fine powder. 2. The particle size of powder can be controlled due to the use of a classifier. 3. There is no wear of the mill and hence there is no contamination of the product. 4. It is useful for grinding heat sensitive substances such as sulphonamides, vitamins and antibiotics
  • 18. EDGE RUNNER MILL Principle: The size reduction is done by crushing (Compression) due to heavy weight of stones and shearing force which is involved during the movement of these stones. Construction It consists of two heavy rollers and a. bed made of stone or granite. The rollers have a central shaft and they revolve on its axis. The rollers are mounted on a horizontal shaft and move around the bed. Working: The material to be ground is put on the bed and with the help of the scrapers 'it is kept in the path of the stone wheels. The material is ground for a definite period and then it is passed through the sieves to get powder of the required size. Uses: Edge runner mill is used for grinding most of tough drugs to fine powder. Disadvantages: Occupies more space Contamination of product with roller is possible Time consuming process Not employed for sticky materials Energy consumption is high.
  • 20. END RUNNER MILL Principle: Size reduction is done by crushing (compression) due to heavy weight of steel pestle. Shearing stress is also involved during the movement of mortar and pestle. Construction: It is considered as mechanical mortar and pestle. It consist of steel mortar which is fixed to Flanged plate. Underneath the flanged plate, a bevelled cog fitting is attached to horizontal shaft bearing a pulley. Hence the plate and mortar can be rotated with the high speed. The pestle is dumb bell shaped so that balancing and efficient grinding by its weight can be achieved. The bottom of pestle is flat rather than round. The pestle carries an arm which is hinged. By this arrangement, the pestle can be raised from mortar to facilitate emptying and cleaning. The narrow central portion of pestle is longer than the band around it. Hence pestle can rise and fall over material in the mortar. Working : The. Material to be ground placed in mortar .The scrapper puts the material in the path of pestle. The mortar revolves at a high speed . The pestle is placed in the mortar. The revolving mortar causes pestle to move. During this process, size reduction is being achieved by Shearing as well as crushing. The material is being collected and passed through a sieve to get a the powder of desired size. Use: It is suitable for fine grinding. Disadvantages: Not suitable for unbroken or slightly broken condition of drug.
  • 22. THEORIES OF SIZE REDUCTION / MILLING A number of theories have been proposed to establish a relationship between energy input and the degree of size reduction produced. 1. Rittinger’s theory 2. Bond’s theory 3. Kick’s theory 4. Walker’s theory
  • 23. RITTINGER’S THEORY Rittinger’s theory suggests that energy required in a size reduction process is proportional to the new surface area produced. where, E = energy required for size reduction KR = Rittinger’s constant Si = initial specific surface area Sn = final specific surface area Application: It is most applicable in size reducing brittle materials undergoing fine milling.
  • 24. BOND’S THEORY Bond’s theory states that the energy used in crack propagation is proportional to the new crack length produced. where, E = energy required for size reduction KB = Bond’s work index di = initial diameter of particles dn = final diameter of particles Application: This law is useful in rough mill sizing. The work index is useful in comparing the efficiency of milling operations.
  • 25. KICK’S THEORY Kick’s theory states that the energy used in deforming (or fracturing) a set of particles of equivalent shape is proportional to the ratio of change of size, or: where, E = energy required for size reduction KK = Kick’s constant di = initial diameter of particles dn = final diameter of particles Application: For crushing of large particles Kick’s theory most useful.
  • 26. WALKER’S THEORY Walker proposed a generalized differential form of the energy- size relationship: where E = amount of energy (work done) required to produce a change D = size of unit mass K = Constant n = constant For n =1.0 Walker equation becomes Kick’s theory used for coarse particles > 1 m. For n =1.5 Walker equation becomes Bond’s theory. This theory is used when neither Kick’s nor Rittinger’s law is applicable. For n =2.0 Walker equation becomes Rittinger’s theory used for fine particles < 1 m size.