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Scale-Up
Techniques for production
of tablets
DEPARTMENT OF PHARMACEUTICS
1
 Pilot Plant:- It is the part of the
pharmaceutical industry where a lab
scale formula is transformed into a
viable product by development of liable
and practical procedure of manufacture.
 Scale-up:- The art for designing of
prototype using the data obtained from
the pilot plant model.
2
Scale up
Laboratory
scale Pilot scale
Large
scale
3
General considerations :
Reporting
Responsibilities
Personal Requirements
Space Requirements
Review of the formula
Raw materials
Relevant Processing
Equipment 4
Production Rates
Process Evaluation
Manufacturing
Procedures
Product stability and
uniformity
Transfer of Analytical
Methods to QA 5
6
Reporting Responsibilities
• R & D with separate staff
• Formulator
Personnel Requirements
• Scientists
• Personnel with engineering
background
Raw materials
• Approved and validated
Space Requirements
Administration and
information processing
Standard equipment
floor space
Physical testing area
Storage area
7
• Purpose of each
ingredient
Review of
formula
• Economical and the
simplest & efficient
Equipment
• Future market
requirements
Production
Rates
8
Process Evaluation
Parameters
order of
mixing
Mixing
time
Mixing
speed
Drying
temp &
time
Screen
size
Rate of
addition
of
agents
9
10
• Weight sheet,
Processing
directions, SOP
Manufacturing
Procedures
Preparation
• Physical and
chemical stability of
the products.
Product
stability and
uniformity
• Quality assurance
staff should review
Transfer of
Analytical
Methods to QA
GMP CONSIDERATION
Equipment qualification
Process validation
Regularly scheduled preventive
maintenance
Regular process review and
revalidation
Relevant written SOP
Technically qualified personnel
Training of personnel
Well defined technology transfer
system
Validated cleaning procedures
Orderly arrangement of equipment 11
Different Methods Of Tablet
Manufacture
12
Wet granulation:
Weighing Milling Granulatio
n
Drying
Blending
Lubrication
Compression
13
DRY GRANULATION
14
Compression
Lubrication
Milling
First Compression
Mixing
Milling
Weighing
Direct compression
Weighing
Milling
Blending
Lubrication
Compression 15
Material handling system
 In Lab scale
 Large Scale depends on
density and static charge
16
Vacuum loading
Scooped, dumped or
poured by hand
Lifting and tilting drums
Vacuum loading systems
Screw feed systems
Metering pumps
Dry Blending
 Powders to be used for granulation must be well
blended to ensure good drug distribution.
 Inadequate blending at this stage could result in
discrete portion of the batch being either high or
low in potency.
 Steps should also be taken to ensure that all the
ingredients are free of lumps and agglomerates.
 SCALE UP CONSIDERATIONS
17
Time of blending .
Blender loading.
Size of blender.
V- cone blender
The equipment used for
blending are:
18
V- cone blender
Double cone
Ribbon blender
Slant cone
blender
Bin blender
Orbiting screw
blenders vertical
and horizontal
high intensity
mixers.
Double cone blender Ribbon blender
19
Granulation
wet granulation has been carried
out by
 Sigma blade mixer,
 Planetary mixer.
20
To impart good flow properties,
increase the density of the powders,
change the particle size,
Uniform dispersion of active ingredient.
Planetary sigma blade
mixer mixer
21
 Wet granulation can also be prepared using
tumble blenders equipped with high-speed
chopper blades
 More recently, the use of multifunctional
“processors” that are capable of performing all
functions required to prepare a finished
granulation, such as dry blending, wet
granulation, drying, sizing and lubrication in a
continuous process in a single equipment.
22
Binders:
23
Make powders more compressible and to
produce tablets that are more resistant to
breakage during handling.
binding agent imparts viscosity to the granulating
solution so that transfer of fluid becomes difficult
This problem can be overcome by adding some or all
binding agents in the dry powder prior to granulation.
 Some granulation, when prepared in production
sized equipment, take on a dough-like
consistency and may have to be subdivided to a
more granular and porous mass to facilitate
drying.
 This can be accomplished by passing the wet
mass through an oscillating type granulator
with a suitably large screen or a hammer mill
with either a suitably large screen or no screen
at all.
24
Drying
 The most common conventional method of drying a
granulation continues to be the circulating hot air
oven, which is heated by either steam or electricity.
 The important factor to consider as part of scale-up
of an oven drying operation are airflow, air
temperature, and the depth of the granulation on the
trays.
 If the granulation bed is too deep or too dense, the
drying process will be inefficient, and if soluble
dyes are involved, migration of the dye to the
surface of the granules.
 Drying times at specified temperatures and airflow
rates must be established for each product, and for
each particular oven load.
25
 Fluidized bed dryers
are an attractive
alternative to the
circulating hot air
ovens.
 The important factor
considered as part of
scale up fluidized bed
dryer are optimum
loads, rate of air flow,
inlet air temperature
and humidity.
26
Milling
 Compression factors that may be affected by the
particle size distribution are flowability,
compressibility, uniformity of tablet weight, content
uniformity, tablet hardness, and tablet color
uniformity.
 First step in this process is to determine the particle
size distribution of granulation using a series of
“stacked” sieves of decreasing mesh openings.
 Particle size reduction of the dried granulation of
production size batches can be carried out by
passing all the material through an oscillating
granulator, a hammer mill, a mechanical sieving
device, or in some cases, a screening device.
27
 As part of the scale-up of a milling or sieving
operation, the lubricants and glidants, which in the
laboratory are usually added directly to the final
blend, are usually added to the dried granulation
during the sizing operation.
 This is done because some of these additives,
especially magnesium stearate, tend to agglomerate
when added in large quantities to the granulation in
a blender.
28
Hammer mill Oscillating type granulator
29
Blending
 Type of blending equipment often differs from
that using in laboratory.
 In any blending operation, both segregation and
mixing occur simultaneously are a function of
particle size, shape, hardness, and density, and
of the dynamics of the mixing action.
 Particle abrasion is more likely to occur when
high-shear mixers with spiral screws or blades
are used.
 When a low dose active ingredient is to be
blended it may be sandwiched between two
portions of directly compressible excipients to
avoid loss to the surface of the blender.
30
 Equipments used for mixing
 Sigma blade mixer.
 Planetary mixer.
 Twin shell blender.
 High shear mixer
31
Slugging (Dry Granulation)
 A dry powder blend that cannot be directly compressed
because of poor flow or compression properties.
 This is done on a tablet press designed for slugging, which
operates at pressures of about 15 tons, compared with a
normal tablet press, which operates at pressure of 4 tons or
less.
 Slugs range in diameter from 1 inch, for the more easily
slugged material, to ¾ inch in diameter for materials that
are more difficult to compress and require more pressure
per unit area to yield satisfactory compacts.
 If an excessive amount of fine powder is generated during
the milling operation the material must be screened & fines
recycled through the slugging operation.
32
Dry Compaction
 Granulation by dry compaction can also be achieved by
passing powders between two rollers that compact the
material at pressure of up to 10 tons per linear inch.
 Materials of very low density require roller compaction
to achieve a bulk density sufficient to allow
encapsulation or compression.
 One of the best examples of this process is the
densification of aluminum hydroxide.
 Pilot plant personnel should determine whether the final
drug blend or the active ingredient could be more
efficiently processed in this manner than by conventional
processing in order to produce a granulation with the
required tabletting or encapsulation properties.
33
34
Compression
 The ultimate test of a tablet formulation and granulation
process is whether the granulation can be compressed on
a high-speed tablet press.
 During compression, the tablet press performs the
following functions:
 Filling of empty die cavity with granulation.
 Precompression of granulation (optional).
 Compression of granules.
 Ejection of the tablet from the die cavity and take-off of
compressed tablet.
35
Tablet Coating
 Sugar coating is carried out in conventional coating pans,
has undergone many changes because of new
developments in coating technology and changes in
safety and environmental regulations.
 The conventional sugar coating pan has given way to
perforated pans or fluidized-bed coating columns.
 The development of new polymeric materials has
resulted in a change from aqueous sugar coating and
more recently, to aqueous film coating.
 The tablets must be sufficiently hard to withstand the
tumbling to which they are subjected in either the coating
pan or the coating column.
36
37
 Some tablet core materials are
naturally hydrophobic, and in
these cases, film coating with an
aqueous system may require
special formulation of the tablet
core and/or the coating solution.
 A film coating solution may
have been found to work well
with a particular tablet in small
lab coating pan but may be
totally unacceptable on a
production scale.
 This is because of increased
pressure & abrasion to which
tablets are subjected when batch
size is large & different in
temperature and humidity to
which tablets are exposed while
coating and drying process.
REFERENCE
 Leon Lachman, Herbert A. Lieberman, The
Theory and Practice of Industrial Pharmacy,
Indian edition 2009, CBS Publishers,
Pg no: 681
 N.K.Jain, pharmaceutical product development,
Indian edition2006, CBS Publishers, Pg no:681
38
Thank
you
39

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Scaleup techniques for production of tablets 212

  • 1. Scale-Up Techniques for production of tablets DEPARTMENT OF PHARMACEUTICS 1
  • 2.  Pilot Plant:- It is the part of the pharmaceutical industry where a lab scale formula is transformed into a viable product by development of liable and practical procedure of manufacture.  Scale-up:- The art for designing of prototype using the data obtained from the pilot plant model. 2
  • 3. Scale up Laboratory scale Pilot scale Large scale 3
  • 4. General considerations : Reporting Responsibilities Personal Requirements Space Requirements Review of the formula Raw materials Relevant Processing Equipment 4
  • 5. Production Rates Process Evaluation Manufacturing Procedures Product stability and uniformity Transfer of Analytical Methods to QA 5
  • 6. 6 Reporting Responsibilities • R & D with separate staff • Formulator Personnel Requirements • Scientists • Personnel with engineering background Raw materials • Approved and validated
  • 7. Space Requirements Administration and information processing Standard equipment floor space Physical testing area Storage area 7
  • 8. • Purpose of each ingredient Review of formula • Economical and the simplest & efficient Equipment • Future market requirements Production Rates 8
  • 10. 10 • Weight sheet, Processing directions, SOP Manufacturing Procedures Preparation • Physical and chemical stability of the products. Product stability and uniformity • Quality assurance staff should review Transfer of Analytical Methods to QA
  • 11. GMP CONSIDERATION Equipment qualification Process validation Regularly scheduled preventive maintenance Regular process review and revalidation Relevant written SOP Technically qualified personnel Training of personnel Well defined technology transfer system Validated cleaning procedures Orderly arrangement of equipment 11
  • 12. Different Methods Of Tablet Manufacture 12
  • 13. Wet granulation: Weighing Milling Granulatio n Drying Blending Lubrication Compression 13
  • 16. Material handling system  In Lab scale  Large Scale depends on density and static charge 16 Vacuum loading Scooped, dumped or poured by hand Lifting and tilting drums Vacuum loading systems Screw feed systems Metering pumps
  • 17. Dry Blending  Powders to be used for granulation must be well blended to ensure good drug distribution.  Inadequate blending at this stage could result in discrete portion of the batch being either high or low in potency.  Steps should also be taken to ensure that all the ingredients are free of lumps and agglomerates.  SCALE UP CONSIDERATIONS 17 Time of blending . Blender loading. Size of blender.
  • 18. V- cone blender The equipment used for blending are: 18 V- cone blender Double cone Ribbon blender Slant cone blender Bin blender Orbiting screw blenders vertical and horizontal high intensity mixers.
  • 19. Double cone blender Ribbon blender 19
  • 20. Granulation wet granulation has been carried out by  Sigma blade mixer,  Planetary mixer. 20 To impart good flow properties, increase the density of the powders, change the particle size, Uniform dispersion of active ingredient.
  • 22.  Wet granulation can also be prepared using tumble blenders equipped with high-speed chopper blades  More recently, the use of multifunctional “processors” that are capable of performing all functions required to prepare a finished granulation, such as dry blending, wet granulation, drying, sizing and lubrication in a continuous process in a single equipment. 22
  • 23. Binders: 23 Make powders more compressible and to produce tablets that are more resistant to breakage during handling. binding agent imparts viscosity to the granulating solution so that transfer of fluid becomes difficult This problem can be overcome by adding some or all binding agents in the dry powder prior to granulation.
  • 24.  Some granulation, when prepared in production sized equipment, take on a dough-like consistency and may have to be subdivided to a more granular and porous mass to facilitate drying.  This can be accomplished by passing the wet mass through an oscillating type granulator with a suitably large screen or a hammer mill with either a suitably large screen or no screen at all. 24
  • 25. Drying  The most common conventional method of drying a granulation continues to be the circulating hot air oven, which is heated by either steam or electricity.  The important factor to consider as part of scale-up of an oven drying operation are airflow, air temperature, and the depth of the granulation on the trays.  If the granulation bed is too deep or too dense, the drying process will be inefficient, and if soluble dyes are involved, migration of the dye to the surface of the granules.  Drying times at specified temperatures and airflow rates must be established for each product, and for each particular oven load. 25
  • 26.  Fluidized bed dryers are an attractive alternative to the circulating hot air ovens.  The important factor considered as part of scale up fluidized bed dryer are optimum loads, rate of air flow, inlet air temperature and humidity. 26
  • 27. Milling  Compression factors that may be affected by the particle size distribution are flowability, compressibility, uniformity of tablet weight, content uniformity, tablet hardness, and tablet color uniformity.  First step in this process is to determine the particle size distribution of granulation using a series of “stacked” sieves of decreasing mesh openings.  Particle size reduction of the dried granulation of production size batches can be carried out by passing all the material through an oscillating granulator, a hammer mill, a mechanical sieving device, or in some cases, a screening device. 27
  • 28.  As part of the scale-up of a milling or sieving operation, the lubricants and glidants, which in the laboratory are usually added directly to the final blend, are usually added to the dried granulation during the sizing operation.  This is done because some of these additives, especially magnesium stearate, tend to agglomerate when added in large quantities to the granulation in a blender. 28
  • 29. Hammer mill Oscillating type granulator 29
  • 30. Blending  Type of blending equipment often differs from that using in laboratory.  In any blending operation, both segregation and mixing occur simultaneously are a function of particle size, shape, hardness, and density, and of the dynamics of the mixing action.  Particle abrasion is more likely to occur when high-shear mixers with spiral screws or blades are used.  When a low dose active ingredient is to be blended it may be sandwiched between two portions of directly compressible excipients to avoid loss to the surface of the blender. 30
  • 31.  Equipments used for mixing  Sigma blade mixer.  Planetary mixer.  Twin shell blender.  High shear mixer 31
  • 32. Slugging (Dry Granulation)  A dry powder blend that cannot be directly compressed because of poor flow or compression properties.  This is done on a tablet press designed for slugging, which operates at pressures of about 15 tons, compared with a normal tablet press, which operates at pressure of 4 tons or less.  Slugs range in diameter from 1 inch, for the more easily slugged material, to ¾ inch in diameter for materials that are more difficult to compress and require more pressure per unit area to yield satisfactory compacts.  If an excessive amount of fine powder is generated during the milling operation the material must be screened & fines recycled through the slugging operation. 32
  • 33. Dry Compaction  Granulation by dry compaction can also be achieved by passing powders between two rollers that compact the material at pressure of up to 10 tons per linear inch.  Materials of very low density require roller compaction to achieve a bulk density sufficient to allow encapsulation or compression.  One of the best examples of this process is the densification of aluminum hydroxide.  Pilot plant personnel should determine whether the final drug blend or the active ingredient could be more efficiently processed in this manner than by conventional processing in order to produce a granulation with the required tabletting or encapsulation properties. 33
  • 34. 34
  • 35. Compression  The ultimate test of a tablet formulation and granulation process is whether the granulation can be compressed on a high-speed tablet press.  During compression, the tablet press performs the following functions:  Filling of empty die cavity with granulation.  Precompression of granulation (optional).  Compression of granules.  Ejection of the tablet from the die cavity and take-off of compressed tablet. 35
  • 36. Tablet Coating  Sugar coating is carried out in conventional coating pans, has undergone many changes because of new developments in coating technology and changes in safety and environmental regulations.  The conventional sugar coating pan has given way to perforated pans or fluidized-bed coating columns.  The development of new polymeric materials has resulted in a change from aqueous sugar coating and more recently, to aqueous film coating.  The tablets must be sufficiently hard to withstand the tumbling to which they are subjected in either the coating pan or the coating column. 36
  • 37. 37  Some tablet core materials are naturally hydrophobic, and in these cases, film coating with an aqueous system may require special formulation of the tablet core and/or the coating solution.  A film coating solution may have been found to work well with a particular tablet in small lab coating pan but may be totally unacceptable on a production scale.  This is because of increased pressure & abrasion to which tablets are subjected when batch size is large & different in temperature and humidity to which tablets are exposed while coating and drying process.
  • 38. REFERENCE  Leon Lachman, Herbert A. Lieberman, The Theory and Practice of Industrial Pharmacy, Indian edition 2009, CBS Publishers, Pg no: 681  N.K.Jain, pharmaceutical product development, Indian edition2006, CBS Publishers, Pg no:681 38