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CENTRIFUGATIO
N
CONTENTS
 Definition of centrifugation
 History
 Principle of centrifugation
 Classification
 Operation
 Construction
 Application in Pharmaceutical industry
 Advantages & disadvantages
 Safety measures
 importance
 Summary
WHAT IS CENTRIFUGATION?
Centrifugation is one of the most important and widely applied research
cellular techniques in bio-chemistry and molecular biology, pharmacy and in
medicine.
 Centrifugation is a process which involves the use of the
centrifugal force for the sedimentation of heterogeneous mixtures
with a centrifuge.
 A centrifuge is a device which consists of a container in which a
mixture of solid and liquid or two liquids is placed and rotated at
high speeds.
 Centrifugal force is an apparent force that acts outward on a body
moving around a center, arising from the body's inertia.
APPLICATIONS
 PRODUCTION OF BULK DRUGS: Separation of crystalline drugs such as
aspirin from mother liquor.
 PRODUCTION OF BIOLOGICAL PRODUCTS: Proteinaceous drugs and
macromolecules – colloidal dispersions in water – Insulin from other
fractions of proteins; blood cells from blood.
 Biopharmaceutical analysis of drugs: Drugs in Blood, tissue fluids and urine
– PK and BE studies.
 Evaluation of Suspensions and emulsions: Creaming – Stable emulsion – no
separation – Centrifuging at 2000 – 3000 rpm at RT.
 Determination of molecular weight: Polymer – serum albumin, insulin, MC
– ultracentrifuge.
THEORY OF CENTRIFUGATION
Particles having above 5 µm sediment due to gravitation force. Lessthan
5 µm particle undergo Brownian motion, they do not sediment under
gravity. Hence a stronger force (Centrifugal force) is applied to separate.
Consider a body of mass m kg rotating in a circular path or radius r mtrs at
a velocity v mtrs per minute. The force acting on the body in a radial
direction is given by :
F= mv2
/ r
Where,
F= Centrifugal force N m= effective mass of the sedimenting particle
v= angular velocity of rotation r= distance of the migrating particles from
the central axis of rotation
The same body is experiencing gravitational force, Gravitational Force G = mg
g = acceleration due to gravity
Centrifugal Effect = F / G = mv2
/ mgr = v2
/ gr
But v = 2 пrn; n = speed of rotation substituting
C = (2 пrn )2
/ gr = 4 п2
r2
n2
/ gr = 4 п2
r n2
Since 2r = d (dia of rotation)
C = 2 п2
d n2
/g
The gravitational constant has a value of 9.807 m/s2
Equation can be written as Centrifugal Effect = 2.013 n2
d
Centrifugal effect α diameter
Centrifugal effect α (speed of rotation) 2
CLASSIFICATION OF CENTRIFUGATION
CLASSIFICATION OF CENTRIFUGATION
BASED ON MECHANISM OF SEPARATION
SEDIMENTATION CENTRIFUGE
ULTRACENTRIFUGE
FILTRATION CENTRIFUGE
BASED ON SCALE OF USAGE
Laboratory scale : Horizontal spinning arm type
Angle Centrifuge (45 to 50 angle)
High speed centrifuge (10,000 rpm)
Ultracentrifuge (85,000 rpm) Commercial Scale
Batch Type: Perforated Basket Type
Semi-continuous Scale : Short-cycle batch centrifuge
Continuous Centrifuge : Supercentrifuge
SEDIMENTATION
CENTRIFUGEUtilizes density difference between the particles and the medium in which
these are dispersed and efficiency depends on velocity of rotation.
Ex :- Horizontal continuous centrifuge, super centrifuge, conical disc
centrifuge.
ULTRA-CENTRIFUGE
In colloidal research, very extremely fine solid material is to be separated.
In this a relatively small motor with speeds exceeding 1,00,000 rpm and
force 1 million times gravity.
Uses: To remove
•Dirt and water from olive & fish liver oils
•Bacteria in the preparation of bacterial enzymes
•Precipitated proteins in manufacture of insulin
Separation of
•Blood plasma from whole blood
•Antibiotics preparation
•Suspensions containing low conc. of solids
•Lanolin from wool
ULTRA-CENTRIFUGE
Advantages and Disadvantages:
•Compact , occupy small space
•Efficiency is very high
•Two immiscible liquids easily separated by continuous process
•By speed control, separated coarser, leaving finer in the suspension.
•Complicated construction
•Limited capacity
FILTRATIONCENTRIFUGE
Solid pass through porous membrane based on density differences. Filter
medium used are canvas or metal cloth. Ex: Perforated basket and semi
continuous centrifuge.
Uses:
•Solid recovery and To remove unwanted solids from liquids ex: insulin
Advantges and Disadvantages: Slurries with high proportions, even paste
•Final product – low moisture content
•Dissolved solids separation from the cake
•Entire cycle complicated – Labour cost is high
•Batch or semi continuous process
•Hard cake formation – removal of cake is difficult
1. Perforated-basket centrifuges
(filtration centrifuge)
Basket – copper, monel or other suitable metal and covered
with vulcanite or lead, greatest resistance to corrosion.
Dia – 0.9m ; capacity – 0.085 m3.
Power – 5 kw for starting and 2 kw for running
Rpm – basket rotates at 1000rpm
Wear and tear, on prolonged operation – hard cake
formation
Cycle is complicated
NON-PERFORATED BASKET
-CENTRIFUGE(SEDIMENTATION CENTRIFUGE)
CONSTRUCTION:
•Basket – steel other suitable metal
•Suspended on vertical shaft
WORKING:
•Solid phase is retained on the sides, liquid remains on the top
•Liquid is removed by weir or skimming tube
•Solids are scraped off by hand or using a scraper blade.
USES:
•When deposited solids offer high resistance to the flow of liquid.
SHORT CYCLE AUTOMATIC BATCH
CENTRIFUGEPRINCIPLE: FILTRATION CENTRIFUGE
WORKING:
•Basket is allowed to rotate and slurry is introduced from the side pipe.
•During centrifugation, slurry passes through the perforated wall.
•Solids retained on the wall, liq collected at outlet.
•Cake is washed with water – washings escape through the filtrate outlet.
•Desired thickness(50-70mm), the feeler cuts off the air supply to a diaphragm
valve that shuts the feed entry.
•Hydraulic cylinder is actuated, lifts the knife along with discharge chute.
•Knife does not cuts the cake completely, leaves a layer to acts as filter medium
for further separation in next cycle.
•The discharge crystals contain 2 to 4 % moisture.
Advantages and Disadvantages:
•Solids drained fast from the bowl.
•Discharge, breakage of crystals
•More Moving parts – complicated construction
CONSTRUCTION:
•Vertical perforated basket supported by horizontal drive
•Provision for feed, wash pipe at center
•Feeler rides over the feed to control the thickness of the cake
•Hydraulic cylinder attachment for entry of discharge chute from the
sides of basket, when discharge of crystals required.
3. Continuous centrifuge
CONTINUOUS HORIZONTAL CENTRIFUGE
PRINCIPLE: SEDIMENTATION CENTRIFUGE
CONSTRUCTION:
•Cylindrical or conical bowl mounted horizontally with dia 0.5m
•Within a bowl screw conveyor is attached – rotates same direction as bowl
but slightly slower speed
WORKING:
•Bowl and screw conveyor are allowed to rotate and slurry is introduced
through the shaft.
•During centrifugation, liq moves to wider portion and sedimentation of
particles takes place.
•Solids are lifted by the screw conveyor, while liq is continuously drained.
•Solids are conveyed to a dry beach where they get dried.
USES: High proportion of solids.
Advantages and Disadvantages:
•Flexible in operation.
•Capable of handling solids larger (10-15mm) or smaller (few microns)
•0.5 to 50% concentrate slurries -use
1. Cylindroconical bowl
2. Helical extraction screw (scroll)
3. Feed
4. Distributor
5. Ring space
6. Settled product
7. Liquid level
8. Drying zone
9. Clarified liquid
10.Adjustable thresholds
CONTINUOUS HORIZONTAL CENTRIFUGE
SUPER CENTRIFUGE
PRINCIPLE: SEDIMENTATION CENTRIFUGE
CONSTRUCTION:
•Long hollow cylindrical bowl – small diameter
•Suspended from a flexible spindle at the top and guided by loose
fit bushing at bottom.
•Feed inlet using pressure – bottom
•Liquid outlets 2 at different heights – top
•Modified wiers are attached.
WORKING:
•Allowed to rotate on its longitudinal axis at higher speed
(2000rpm) with help of drive assembly.
•Feed is introduced at the bottom with pressure
•During centrifugation the heavier liq thrown outward (against
wall), lighter liq forms an inner layer. Both liq rise to top
•The liq –liq interface is maintained by an hydraulic balance.
•Thus, 2 layers are separated continuously by modified wiers
USE : Emulsions
Variant:
•Tubular bowl centrifuge – separation of solids and liquids
2. Tubular-bowl centrifuges
(centrifugal sedimenters)
Fig: Tubular-bowl centrifuge
CONICAL DISC CENTRIFUGE or DE LAVAL CLARIFIER
(Sedimentation Centrifugation)
Clarifier, solids or immiscible liquids are present in low conc. A no. of cone
shaped plates are attached to a central shaft (Feed provisions). Dense solids
are thrown outwards – underside of the cone shaped casing, lighter
clarified liq passes over the bowl and recovered from the top of the cone
CONSTRUCTION:
•shallow bowl – series of conical discs – to
centre shaft at diff elevations
•Disc – thin sheet of metal or plastic separated
by narrow spaces.
WORKING:
•Allowed to rotate on its longitudinal axis at
low speed and short time
•During centrifugation the heavier liq thrown
outward (against wall), lighter liq forms an
inner layer. Both liq rise to top
•Substances moves along the surface of the
disc to the limit of inner and outer layers.
•Solids deposit at bottom of cone, removed
intermittently
• Matching holes in disc – channels to
pass the liq.
• A concentric tube is placed
surrounding the central drive shaft.
(Feed entry)
USES:
•Immiscible liq separation – Mfr of antibiotics
•Suspensions containing low solids
•Solids – gelatinous or slimy – separated
•Collection od starch
•Insulin
•Concentration of one fluid phase – separation of cream from milk
ADVANTAGES:
•Small space occupying
•Separation efficiency – high, particles are sediment very rapidly
•Suitable – fluid is deposit or sludge
•By controlling speed of rotation and rate of flow – particles are separated into two size
fractions.
DISADVANTAGES: Complicated construction , Limited capacity
•Not suitable for hard cake forming solids
Fabrication: Carbon fiber, Aluminum and
Titanium.
Some Other Commercial
applications
in water and wastewater treatment to dry sludge.
from the mother liquor .
 In soil mechanics.
 Large industrial centrifuges are commonly used
 In sugar industry to separate the sugar crystals
 Standalone centrifuges for drying (hand-washed)
clothes – usually with a water outlet.
 Large industrial centrifuges are also used in the
oil industry to remove solids from the drilling
fluid.
 Centrifuges are used in the attraction Mission
ADVANTAGES AND
DISADVANTAGES:
Advantages:
 Centrifuges have a clean appearance and have little to no odor
problems.
 Not only is the device easy to install and fast at starting up
and shutting down, but also only requires a small area for
operation.
 They can be selected for different applications. .
 The device is simple to operate .
 Centrifuge has more process flexibility and higher levels of
performance.
DISADVANTAGES:
 The machine can be very noisy and can
cause vibration.
 The device has a high-energy consumption
due to high G-forces.
 High initial capital costs
SAFETY MEASURES
A centrifuge user should strictly observe the following
precautions :
 Manufacturer’s manual should be strictly followed.
 Rotor should be stored in proper containers.
 Attention should be given to imbalance detectors.
 Rotor speed should not exceed the assigned speed.
 Lid of the rotor chamber should remain locked during
operation.
 To avoid the rotor failure, manufactures instructions
regarding rotor care and use should always be
followed.
SUMMARY
 The centrifugation is a modern & easy
technique of separation and sedimentation on
the basis of shape, size and density of
macromolecules and other particles.
 In the centrifugation there are different types
of forces are applied like as centrifugal force,
gravitational force and centripetal force etc.
and also different types of rotors are to be
used that is; Swinging Bucket Rotor and fixed
angle rotors at different RPM/RCF.
IMPORTANCE
Centrifugation play an important
role in both biological sectors as
well as industrial sectors.
In biological sector:
 Medical laboratories use
centrifuges to separate plasma
from heavier blood cells.
 Modern centrifuges can even
separate mixtures of different
sized molecules or microscopic
particles such as parts of cells.
Continued…..
In Industrial Sector:
 Cream separation from milk.
 Separating textiles
 Separating particles from an air flow using
cyclonic separation
 Clarification and stabilization of wine
 Centrifugation is the most common method
used for uranium enrichment.
REFERENCES
http://www.labmanager.com/lab-product/2010/05/evolution-of-the-lab-
centrifuge?fw1pk=2#.Viz08yskqxn
http://www.westernstates.com/continuous-centrifuges
https://en.wikipedia.org/wiki/Centrifuge
https://en.wikipedia.org/wiki/Differential_centrifugation
http://cellbiologyolm.stevegallik.org/node/74
 D. Rickwood and J. M. Graham (2001); Biological Centrifugation,
Springer Verlag; ISBN: 0387915761.
 D. Rickwood, T. Ford, J. Steensgaard (1994): John Wiley & Son Ltd.
ISBN: 0471942715.
 T. C. Ford and J. M. Graham (1991): An Introduction to Centrifugation,
BIOS Scientific Publishers, Ltd. ISBN 1 872748 40 6.
 http://www.thermoscientific.com/content/dam/tfs/LPG/LED/LED%20
Documents/Third-
Party%20Papers/Centrifuges/Centrifuge%20Rotors/Ultracentrifuge%20R
otors/D20940~.pdf
Centrifugation Technique for Separating Pharmaceutical Mixtures

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Centrifugation Technique for Separating Pharmaceutical Mixtures

  • 2. CONTENTS  Definition of centrifugation  History  Principle of centrifugation  Classification  Operation  Construction  Application in Pharmaceutical industry  Advantages & disadvantages  Safety measures  importance  Summary
  • 3. WHAT IS CENTRIFUGATION? Centrifugation is one of the most important and widely applied research cellular techniques in bio-chemistry and molecular biology, pharmacy and in medicine.  Centrifugation is a process which involves the use of the centrifugal force for the sedimentation of heterogeneous mixtures with a centrifuge.  A centrifuge is a device which consists of a container in which a mixture of solid and liquid or two liquids is placed and rotated at high speeds.  Centrifugal force is an apparent force that acts outward on a body moving around a center, arising from the body's inertia.
  • 4. APPLICATIONS  PRODUCTION OF BULK DRUGS: Separation of crystalline drugs such as aspirin from mother liquor.  PRODUCTION OF BIOLOGICAL PRODUCTS: Proteinaceous drugs and macromolecules – colloidal dispersions in water – Insulin from other fractions of proteins; blood cells from blood.  Biopharmaceutical analysis of drugs: Drugs in Blood, tissue fluids and urine – PK and BE studies.  Evaluation of Suspensions and emulsions: Creaming – Stable emulsion – no separation – Centrifuging at 2000 – 3000 rpm at RT.  Determination of molecular weight: Polymer – serum albumin, insulin, MC – ultracentrifuge.
  • 5. THEORY OF CENTRIFUGATION Particles having above 5 µm sediment due to gravitation force. Lessthan 5 µm particle undergo Brownian motion, they do not sediment under gravity. Hence a stronger force (Centrifugal force) is applied to separate. Consider a body of mass m kg rotating in a circular path or radius r mtrs at a velocity v mtrs per minute. The force acting on the body in a radial direction is given by : F= mv2 / r Where, F= Centrifugal force N m= effective mass of the sedimenting particle v= angular velocity of rotation r= distance of the migrating particles from the central axis of rotation The same body is experiencing gravitational force, Gravitational Force G = mg g = acceleration due to gravity
  • 6. Centrifugal Effect = F / G = mv2 / mgr = v2 / gr But v = 2 пrn; n = speed of rotation substituting C = (2 пrn )2 / gr = 4 п2 r2 n2 / gr = 4 п2 r n2 Since 2r = d (dia of rotation) C = 2 п2 d n2 /g The gravitational constant has a value of 9.807 m/s2 Equation can be written as Centrifugal Effect = 2.013 n2 d Centrifugal effect α diameter Centrifugal effect α (speed of rotation) 2
  • 8. CLASSIFICATION OF CENTRIFUGATION BASED ON MECHANISM OF SEPARATION SEDIMENTATION CENTRIFUGE ULTRACENTRIFUGE FILTRATION CENTRIFUGE BASED ON SCALE OF USAGE Laboratory scale : Horizontal spinning arm type Angle Centrifuge (45 to 50 angle) High speed centrifuge (10,000 rpm) Ultracentrifuge (85,000 rpm) Commercial Scale Batch Type: Perforated Basket Type Semi-continuous Scale : Short-cycle batch centrifuge Continuous Centrifuge : Supercentrifuge
  • 9. SEDIMENTATION CENTRIFUGEUtilizes density difference between the particles and the medium in which these are dispersed and efficiency depends on velocity of rotation. Ex :- Horizontal continuous centrifuge, super centrifuge, conical disc centrifuge. ULTRA-CENTRIFUGE In colloidal research, very extremely fine solid material is to be separated. In this a relatively small motor with speeds exceeding 1,00,000 rpm and force 1 million times gravity. Uses: To remove •Dirt and water from olive & fish liver oils •Bacteria in the preparation of bacterial enzymes •Precipitated proteins in manufacture of insulin Separation of •Blood plasma from whole blood •Antibiotics preparation •Suspensions containing low conc. of solids •Lanolin from wool
  • 10. ULTRA-CENTRIFUGE Advantages and Disadvantages: •Compact , occupy small space •Efficiency is very high •Two immiscible liquids easily separated by continuous process •By speed control, separated coarser, leaving finer in the suspension. •Complicated construction •Limited capacity FILTRATIONCENTRIFUGE Solid pass through porous membrane based on density differences. Filter medium used are canvas or metal cloth. Ex: Perforated basket and semi continuous centrifuge. Uses: •Solid recovery and To remove unwanted solids from liquids ex: insulin Advantges and Disadvantages: Slurries with high proportions, even paste •Final product – low moisture content •Dissolved solids separation from the cake •Entire cycle complicated – Labour cost is high •Batch or semi continuous process •Hard cake formation – removal of cake is difficult
  • 12. Basket – copper, monel or other suitable metal and covered with vulcanite or lead, greatest resistance to corrosion. Dia – 0.9m ; capacity – 0.085 m3. Power – 5 kw for starting and 2 kw for running Rpm – basket rotates at 1000rpm
  • 13. Wear and tear, on prolonged operation – hard cake formation Cycle is complicated
  • 14. NON-PERFORATED BASKET -CENTRIFUGE(SEDIMENTATION CENTRIFUGE) CONSTRUCTION: •Basket – steel other suitable metal •Suspended on vertical shaft WORKING: •Solid phase is retained on the sides, liquid remains on the top •Liquid is removed by weir or skimming tube •Solids are scraped off by hand or using a scraper blade. USES: •When deposited solids offer high resistance to the flow of liquid.
  • 15. SHORT CYCLE AUTOMATIC BATCH CENTRIFUGEPRINCIPLE: FILTRATION CENTRIFUGE WORKING: •Basket is allowed to rotate and slurry is introduced from the side pipe. •During centrifugation, slurry passes through the perforated wall. •Solids retained on the wall, liq collected at outlet. •Cake is washed with water – washings escape through the filtrate outlet. •Desired thickness(50-70mm), the feeler cuts off the air supply to a diaphragm valve that shuts the feed entry. •Hydraulic cylinder is actuated, lifts the knife along with discharge chute. •Knife does not cuts the cake completely, leaves a layer to acts as filter medium for further separation in next cycle. •The discharge crystals contain 2 to 4 % moisture. Advantages and Disadvantages: •Solids drained fast from the bowl. •Discharge, breakage of crystals •More Moving parts – complicated construction
  • 16. CONSTRUCTION: •Vertical perforated basket supported by horizontal drive •Provision for feed, wash pipe at center •Feeler rides over the feed to control the thickness of the cake •Hydraulic cylinder attachment for entry of discharge chute from the sides of basket, when discharge of crystals required.
  • 17.
  • 19. CONTINUOUS HORIZONTAL CENTRIFUGE PRINCIPLE: SEDIMENTATION CENTRIFUGE CONSTRUCTION: •Cylindrical or conical bowl mounted horizontally with dia 0.5m •Within a bowl screw conveyor is attached – rotates same direction as bowl but slightly slower speed WORKING: •Bowl and screw conveyor are allowed to rotate and slurry is introduced through the shaft. •During centrifugation, liq moves to wider portion and sedimentation of particles takes place. •Solids are lifted by the screw conveyor, while liq is continuously drained. •Solids are conveyed to a dry beach where they get dried. USES: High proportion of solids. Advantages and Disadvantages: •Flexible in operation. •Capable of handling solids larger (10-15mm) or smaller (few microns) •0.5 to 50% concentrate slurries -use
  • 20. 1. Cylindroconical bowl 2. Helical extraction screw (scroll) 3. Feed 4. Distributor 5. Ring space 6. Settled product 7. Liquid level 8. Drying zone 9. Clarified liquid 10.Adjustable thresholds CONTINUOUS HORIZONTAL CENTRIFUGE
  • 21. SUPER CENTRIFUGE PRINCIPLE: SEDIMENTATION CENTRIFUGE CONSTRUCTION: •Long hollow cylindrical bowl – small diameter •Suspended from a flexible spindle at the top and guided by loose fit bushing at bottom. •Feed inlet using pressure – bottom •Liquid outlets 2 at different heights – top •Modified wiers are attached. WORKING: •Allowed to rotate on its longitudinal axis at higher speed (2000rpm) with help of drive assembly. •Feed is introduced at the bottom with pressure •During centrifugation the heavier liq thrown outward (against wall), lighter liq forms an inner layer. Both liq rise to top •The liq –liq interface is maintained by an hydraulic balance. •Thus, 2 layers are separated continuously by modified wiers USE : Emulsions Variant: •Tubular bowl centrifuge – separation of solids and liquids
  • 24. CONICAL DISC CENTRIFUGE or DE LAVAL CLARIFIER (Sedimentation Centrifugation) Clarifier, solids or immiscible liquids are present in low conc. A no. of cone shaped plates are attached to a central shaft (Feed provisions). Dense solids are thrown outwards – underside of the cone shaped casing, lighter clarified liq passes over the bowl and recovered from the top of the cone CONSTRUCTION: •shallow bowl – series of conical discs – to centre shaft at diff elevations •Disc – thin sheet of metal or plastic separated by narrow spaces. WORKING: •Allowed to rotate on its longitudinal axis at low speed and short time •During centrifugation the heavier liq thrown outward (against wall), lighter liq forms an inner layer. Both liq rise to top •Substances moves along the surface of the disc to the limit of inner and outer layers. •Solids deposit at bottom of cone, removed intermittently • Matching holes in disc – channels to pass the liq. • A concentric tube is placed surrounding the central drive shaft. (Feed entry)
  • 25. USES: •Immiscible liq separation – Mfr of antibiotics •Suspensions containing low solids •Solids – gelatinous or slimy – separated •Collection od starch •Insulin •Concentration of one fluid phase – separation of cream from milk ADVANTAGES: •Small space occupying •Separation efficiency – high, particles are sediment very rapidly •Suitable – fluid is deposit or sludge •By controlling speed of rotation and rate of flow – particles are separated into two size fractions. DISADVANTAGES: Complicated construction , Limited capacity •Not suitable for hard cake forming solids
  • 26. Fabrication: Carbon fiber, Aluminum and Titanium.
  • 27.
  • 28. Some Other Commercial applications in water and wastewater treatment to dry sludge. from the mother liquor .  In soil mechanics.  Large industrial centrifuges are commonly used  In sugar industry to separate the sugar crystals  Standalone centrifuges for drying (hand-washed) clothes – usually with a water outlet.  Large industrial centrifuges are also used in the oil industry to remove solids from the drilling fluid.  Centrifuges are used in the attraction Mission
  • 29. ADVANTAGES AND DISADVANTAGES: Advantages:  Centrifuges have a clean appearance and have little to no odor problems.  Not only is the device easy to install and fast at starting up and shutting down, but also only requires a small area for operation.  They can be selected for different applications. .  The device is simple to operate .  Centrifuge has more process flexibility and higher levels of performance.
  • 30. DISADVANTAGES:  The machine can be very noisy and can cause vibration.  The device has a high-energy consumption due to high G-forces.  High initial capital costs
  • 31. SAFETY MEASURES A centrifuge user should strictly observe the following precautions :  Manufacturer’s manual should be strictly followed.  Rotor should be stored in proper containers.  Attention should be given to imbalance detectors.  Rotor speed should not exceed the assigned speed.  Lid of the rotor chamber should remain locked during operation.  To avoid the rotor failure, manufactures instructions regarding rotor care and use should always be followed.
  • 32. SUMMARY  The centrifugation is a modern & easy technique of separation and sedimentation on the basis of shape, size and density of macromolecules and other particles.  In the centrifugation there are different types of forces are applied like as centrifugal force, gravitational force and centripetal force etc. and also different types of rotors are to be used that is; Swinging Bucket Rotor and fixed angle rotors at different RPM/RCF.
  • 33. IMPORTANCE Centrifugation play an important role in both biological sectors as well as industrial sectors. In biological sector:  Medical laboratories use centrifuges to separate plasma from heavier blood cells.  Modern centrifuges can even separate mixtures of different sized molecules or microscopic particles such as parts of cells.
  • 34. Continued….. In Industrial Sector:  Cream separation from milk.  Separating textiles  Separating particles from an air flow using cyclonic separation  Clarification and stabilization of wine  Centrifugation is the most common method used for uranium enrichment.
  • 35. REFERENCES http://www.labmanager.com/lab-product/2010/05/evolution-of-the-lab- centrifuge?fw1pk=2#.Viz08yskqxn http://www.westernstates.com/continuous-centrifuges https://en.wikipedia.org/wiki/Centrifuge https://en.wikipedia.org/wiki/Differential_centrifugation http://cellbiologyolm.stevegallik.org/node/74  D. Rickwood and J. M. Graham (2001); Biological Centrifugation, Springer Verlag; ISBN: 0387915761.  D. Rickwood, T. Ford, J. Steensgaard (1994): John Wiley & Son Ltd. ISBN: 0471942715.  T. C. Ford and J. M. Graham (1991): An Introduction to Centrifugation, BIOS Scientific Publishers, Ltd. ISBN 1 872748 40 6.  http://www.thermoscientific.com/content/dam/tfs/LPG/LED/LED%20 Documents/Third- Party%20Papers/Centrifuges/Centrifuge%20Rotors/Ultracentrifuge%20R otors/D20940~.pdf