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PREPARED BY: ANKITA YAGNIK
ASSISTANT PROFESSOR
AKSHAR-PREET INSTITUTE OF PHARMACY,
JAMANAGR
Definition
 Centrifugation is a process used to separate or
concentrate materials suspended in a liquid medium.
 The theoretical basis of this technique is the effect of
gravity on particles in suspension.
 Two particles of different masses will settle in a tube
at different rates in response to gravity.
2 ANKITA YAGNIK, APIP
Principle and theory of centrifugation
 Centrifugal effect:
Centrifugal force in terms of the ratio to the gravitational
force is known as centrifugal effect.
 Consider a body of mass m rotating in a circular path of
radius r at a velocity v. The force acting on the body in a
radial direction is given by:
 F = mv2
r
Here, F = centrifugal force
m = mass of the body
v = velocity of body
r = radius of circle of rotation
3 ANKITA YAGNIK, APIP
 The same body will be acted upon by a gravitational force. It
can be expressed as:
G = mg
where, G = gravitational force g = gravitational constant
 The centrifugal effect is the ratio of the two forces, so that:
C = F / G
= mv2 / mgr
= v2 / gr
But, v = 2πrn Where, n = speed of rotation.
So,
F / G = (2πrn)2 / gr
= 4π2r2n2 / gr
= 2 π2n2d / g ……………(1)
Where, d = diameter of rotation.
4 ANKITA YAGNIK, APIP
 The gravitational constant has a value of 9.807 m/s2,
so that equation (1) may be simplified to:
 Centrifugal effect = 2.013 n2d
 Provided that , n is expressed in S-1 and d is in
meter.
 From the equation, it can be drawn that the
centrifugal effect is directly proportional to the
diameter, but is proportional to the square of the
speed of the rotation.
 Thus, if it is necessary to increase the centrifugal
effect, it is of greater advantages to use a centrifuge
of the same size at a higher speed, rather than use a
larger centrifuge at the same speed of rotation.5 ANKITA YAGNIK, APIP
Factors affecting centrifugation process
 Liquid viscosity
 Liquid density
 Solids concentration
 Particle size distribution
 Surface charge of particles
 Type and shape of particles
 Feed rate
 Agitation speed
 Size of centrifuge
 Height of cake
 Mode of operation
 Time at full speed
6 ANKITA YAGNIK, APIP
Classification of centrifuge
Industrial centrifuges can be classified into 3 main types:
(1)Filtration centrifuge:
Those using perforated baskets, which perform a filtration
type operation (work like a spin dryer).
 E.g. perforated basket centrifuge, semi-continuous
centrifuge
(2) Sedimentation centrifuge:
Those with a solid walled vessel, where particles sediment
towards the wall under the influence of the centrifugal
force.
 E.g. Tubular bowl centrifuge, Non-perforated basket
centrifuge, super centrifuge, conical disc centrifuge
(3) Continuous centrifuge:
Those where a continuous process or very high capacity is
required.
E.g. Continuous horizontal centrifuge7 ANKITA YAGNIK, APIP
Perforated basket centrifuge
 Principle:
 Perforated basket centrifuge is a filtration centrifuge.
The separation is through a perforated wall based on
the difference in the densities of solid and liquid
phases.
 The bowl contains a perforated side-wall. During
centrifugation, the liquid phase passes through the
perforated wall while solid phase is retained in the
bowl.
 The solid is removed by a blade.
 In this centrifuge a basket is mounted above a
driving shaft such arrangement is described as
under-driven.8 ANKITA YAGNIK, APIP
 Construction:
 It consist of perforated basket which is made up of
stainless steel and lined with filter cloth.
 The basket is suspended above the shaft and driven
by a motor or turbine.
 Surrounding the basket casing is provided which
collect the filtrate and discharge them to the outlets.
9 ANKITA YAGNIK, APIP
10 ANKITA YAGNIK, APIP
 Working:
 Liquid feed is inserted to the bowl/basket when it is
stationary in such a way that it distributes evenly in
the basket.
 Power is supplied to start the rotation of basket. The
basket should achieve its maximum speed quickly. It
rotates at 1000 rpm.
 During the process liquid passes through perforated
walls and solid remains inside the wall.
 The solid is collected after drying by spinning and
liquid is collected from outlet.
11 ANKITA YAGNIK, APIP
12 ANKITA YAGNIK, APIP
Semi continuous centrifuge
 It is also known as short cycle automatic batch
centrifuge.
 Principle:
 This centrifuge is a filtration centrifuge. The
separation is through a perforated wall based on the
difference in the densities of solid and liquid phases.
 The bowl contains a perforated side-wall. During
centrifugation, the liquid phase passes through the
perforated wall while solid phase is retained in the
bowl.
 The solid is removed by cutting with a blade.
13 ANKITA YAGNIK, APIP
 Working:
 The perforated basket is allowed to rotate and Liquid
feed is inserted to the bowl/basket from side pipe in such
a way that it distributes evenly in the basket.
 During the process liquid passes through perforated walls
and solid remains inside the wall.
 The cake is washed with water. The wash escapes from
the basket through the filtrate outlet.
 The solid is collected after drying by spinning and liquid is
collected from outlet.
 In this centrifuge after achieving the desired thickness
about 50 to 70 mm the feeler cuts off the air supply to
diaphragm valve that automatically cuts of the entry of
the slurry.
14 ANKITA YAGNIK, APIP
ANKITA YAGNIK, APIP15
16 ANKITA YAGNIK, APIP
Non-perforated basket centrifuge
ANKITA YAGNIK, APIP17
 Principle:
 This is sedimentation type centrifuge so separation
takes place on the basis of difference in their
densities without presence of perforated/porous
medium.
 During centrifugation solid remains at side wall of the
basket while liquid remains at the top which is
collected by skimming tube.
Construction:
 It consist of basket made up of stainless steel. The
basket is placed on the vertical shaft.
 Basket contains inlet tube and skimming tube.
ANKITA YAGNIK, APIP18
ANKITA YAGNIK, APIP19
 Working:
 The suspension is fed continuously into the basket.
During centrifugation solid phase is retained on the sides
of the wall while liquid remains on the top.
 The liquid is collected with skimming tube and solids are
scraped off by using scrapper from the basket.
 Uses:
 It is useful when the deposited solids offer high
resistance to the flow of liquid.
 Advantages:
 Cost is less than other centrifuges
 Disadvantages:
 Solid phase is retained on the sides of the basket.
Super centrifuge
ANKITA YAGNIK, APIP20
 Principle:
 This is sedimentation type centrifuge so separation
takes place on the basis of difference in their
densities between to immiscible liquids.
 Centrifugation is done in the bowl of small centrifuge.
During centrifugation the heavier liquid is thrown
against the wall, while lighter liquid remains as inner
layer.
 The two layers are simultaneously separated using
modified wiers.
ANKITA YAGNIK, APIP21
ANKITA YAGNIK, APIP22
ANKITA YAGNIK, APIP23
 Uses:
 Used for separating liquid phase of emulsion in foods and
pharmaceuticals.
 Advantage:
 Continuous operation.
 Can handle much higher concentration.
 Produces dry solids.
 Disadvantage:
 Sediment does not have uniform structure.
ANKITA YAGNIK, APIP24

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Centrifugation by ankita yagnik

  • 1. PREPARED BY: ANKITA YAGNIK ASSISTANT PROFESSOR AKSHAR-PREET INSTITUTE OF PHARMACY, JAMANAGR
  • 2. Definition  Centrifugation is a process used to separate or concentrate materials suspended in a liquid medium.  The theoretical basis of this technique is the effect of gravity on particles in suspension.  Two particles of different masses will settle in a tube at different rates in response to gravity. 2 ANKITA YAGNIK, APIP
  • 3. Principle and theory of centrifugation  Centrifugal effect: Centrifugal force in terms of the ratio to the gravitational force is known as centrifugal effect.  Consider a body of mass m rotating in a circular path of radius r at a velocity v. The force acting on the body in a radial direction is given by:  F = mv2 r Here, F = centrifugal force m = mass of the body v = velocity of body r = radius of circle of rotation 3 ANKITA YAGNIK, APIP
  • 4.  The same body will be acted upon by a gravitational force. It can be expressed as: G = mg where, G = gravitational force g = gravitational constant  The centrifugal effect is the ratio of the two forces, so that: C = F / G = mv2 / mgr = v2 / gr But, v = 2πrn Where, n = speed of rotation. So, F / G = (2πrn)2 / gr = 4π2r2n2 / gr = 2 π2n2d / g ……………(1) Where, d = diameter of rotation. 4 ANKITA YAGNIK, APIP
  • 5.  The gravitational constant has a value of 9.807 m/s2, so that equation (1) may be simplified to:  Centrifugal effect = 2.013 n2d  Provided that , n is expressed in S-1 and d is in meter.  From the equation, it can be drawn that the centrifugal effect is directly proportional to the diameter, but is proportional to the square of the speed of the rotation.  Thus, if it is necessary to increase the centrifugal effect, it is of greater advantages to use a centrifuge of the same size at a higher speed, rather than use a larger centrifuge at the same speed of rotation.5 ANKITA YAGNIK, APIP
  • 6. Factors affecting centrifugation process  Liquid viscosity  Liquid density  Solids concentration  Particle size distribution  Surface charge of particles  Type and shape of particles  Feed rate  Agitation speed  Size of centrifuge  Height of cake  Mode of operation  Time at full speed 6 ANKITA YAGNIK, APIP
  • 7. Classification of centrifuge Industrial centrifuges can be classified into 3 main types: (1)Filtration centrifuge: Those using perforated baskets, which perform a filtration type operation (work like a spin dryer).  E.g. perforated basket centrifuge, semi-continuous centrifuge (2) Sedimentation centrifuge: Those with a solid walled vessel, where particles sediment towards the wall under the influence of the centrifugal force.  E.g. Tubular bowl centrifuge, Non-perforated basket centrifuge, super centrifuge, conical disc centrifuge (3) Continuous centrifuge: Those where a continuous process or very high capacity is required. E.g. Continuous horizontal centrifuge7 ANKITA YAGNIK, APIP
  • 8. Perforated basket centrifuge  Principle:  Perforated basket centrifuge is a filtration centrifuge. The separation is through a perforated wall based on the difference in the densities of solid and liquid phases.  The bowl contains a perforated side-wall. During centrifugation, the liquid phase passes through the perforated wall while solid phase is retained in the bowl.  The solid is removed by a blade.  In this centrifuge a basket is mounted above a driving shaft such arrangement is described as under-driven.8 ANKITA YAGNIK, APIP
  • 9.  Construction:  It consist of perforated basket which is made up of stainless steel and lined with filter cloth.  The basket is suspended above the shaft and driven by a motor or turbine.  Surrounding the basket casing is provided which collect the filtrate and discharge them to the outlets. 9 ANKITA YAGNIK, APIP
  • 11.  Working:  Liquid feed is inserted to the bowl/basket when it is stationary in such a way that it distributes evenly in the basket.  Power is supplied to start the rotation of basket. The basket should achieve its maximum speed quickly. It rotates at 1000 rpm.  During the process liquid passes through perforated walls and solid remains inside the wall.  The solid is collected after drying by spinning and liquid is collected from outlet. 11 ANKITA YAGNIK, APIP
  • 13. Semi continuous centrifuge  It is also known as short cycle automatic batch centrifuge.  Principle:  This centrifuge is a filtration centrifuge. The separation is through a perforated wall based on the difference in the densities of solid and liquid phases.  The bowl contains a perforated side-wall. During centrifugation, the liquid phase passes through the perforated wall while solid phase is retained in the bowl.  The solid is removed by cutting with a blade. 13 ANKITA YAGNIK, APIP
  • 14.  Working:  The perforated basket is allowed to rotate and Liquid feed is inserted to the bowl/basket from side pipe in such a way that it distributes evenly in the basket.  During the process liquid passes through perforated walls and solid remains inside the wall.  The cake is washed with water. The wash escapes from the basket through the filtrate outlet.  The solid is collected after drying by spinning and liquid is collected from outlet.  In this centrifuge after achieving the desired thickness about 50 to 70 mm the feeler cuts off the air supply to diaphragm valve that automatically cuts of the entry of the slurry. 14 ANKITA YAGNIK, APIP
  • 17. Non-perforated basket centrifuge ANKITA YAGNIK, APIP17  Principle:  This is sedimentation type centrifuge so separation takes place on the basis of difference in their densities without presence of perforated/porous medium.  During centrifugation solid remains at side wall of the basket while liquid remains at the top which is collected by skimming tube. Construction:  It consist of basket made up of stainless steel. The basket is placed on the vertical shaft.  Basket contains inlet tube and skimming tube.
  • 19. ANKITA YAGNIK, APIP19  Working:  The suspension is fed continuously into the basket. During centrifugation solid phase is retained on the sides of the wall while liquid remains on the top.  The liquid is collected with skimming tube and solids are scraped off by using scrapper from the basket.  Uses:  It is useful when the deposited solids offer high resistance to the flow of liquid.  Advantages:  Cost is less than other centrifuges  Disadvantages:  Solid phase is retained on the sides of the basket.
  • 20. Super centrifuge ANKITA YAGNIK, APIP20  Principle:  This is sedimentation type centrifuge so separation takes place on the basis of difference in their densities between to immiscible liquids.  Centrifugation is done in the bowl of small centrifuge. During centrifugation the heavier liquid is thrown against the wall, while lighter liquid remains as inner layer.  The two layers are simultaneously separated using modified wiers.
  • 23. ANKITA YAGNIK, APIP23  Uses:  Used for separating liquid phase of emulsion in foods and pharmaceuticals.  Advantage:  Continuous operation.  Can handle much higher concentration.  Produces dry solids.  Disadvantage:  Sediment does not have uniform structure.