Granulation Flashcards

1
Q

Segregation due to particle size - 3 types

A

• Trajectory segregation
– Larger particles travel greater horizontal distances than smaller particles
• Elutriation Segregation
– Very small particles sediment on top of the larger
particles
• Percolation Segregation
– Smaller particles drop to the bottom of the powder bed (as in hopper where movement of particles can take place)

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2
Q

Segregation due to particle density

A
  • Dense particles have tendency to move to bottom

* Dense particles have greater mass than less dense particles

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3
Q

Reasons for granulation

A
  • Help improve powder flow (increase in particle size) - MAIN REASON
  • Help provide a uniform mix of powders
  • Increase density of the powder mix
  • Reduce risks of dust generation
  • Reduces risk of caking of hygroscopic powders (powders draw in water which results in caking)
  • As a dosage form
  • As intermediate for tableting / capsulation (granules used for tableting - easier)
  • Help compaction of powder mix
  • Aid wetting of particles (used when its hydrophobic to make it solubilised)
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4
Q

Considerations

A

• Mixing of powders granule formation
• Segregation of constituents after mixing
• Segregation of constituents after granule formation
• Size distribution of granules
• Tableting and capsulation
– Fill by volume not weight
• Accurate proportions of active ingredient and excipients

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5
Q

Segregation more likely to occur when..

A

particles are different sizes

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6
Q

Wet granulation (most commonly used)

A

• Liquids used in granulation process
– Granulating fluid
• Solvents: water, ethanol, isopropanol
• Compatible
• Non-toxic
• Removable by drying
– Binder
• To help particles adhere together after drying
• Aggregation of primary powder particles to form granules using granulating fluid
• Mixing of powders
• Addition of granulating fluid
• Aggregation of powder particles (wet massing) – Controlled by altering fluid volume added and
intensity/duration of mixing
• Wet mass forced through sieve producing wet granules (granulation)
• Drying stage (different methods available)
• Milling stage (selecting desirable size of
particles for application) – Screening

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7
Q

4 stages of wet granulation

A
  1. Pendular state
  2. Funicular state
  3. Capillary state (ideal)
  4. Droplet state
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8
Q

Formation of liquid bridges between particles

A
  1. Pendular state
    – Low liquid levels, discrete liquid bridges at points of contact between particles
    – Assumption that there is a uniform distribution of liquid throughout powder bed
  2. Funicular state
    – Further liquid content, pendular bonds coalesce and liquid bridges form between non-touching points
    – Dependant on degree of liquid (or voidage) saturation, usually 25-80%
  3. Capillary state
    - Liquid saturation>80%
    - Granule becomes paste-like and unsuitable for wet sieving
    - Tensile strength of granule increases x3 between pendular and capillary state
  4. Droplet state
    - ↑liquid converts capillary state into droplet state (undesirable)
    - Particle completely enclosed in water droplet and mass takes on slurry like properties
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9
Q

What would happen is droplet stage was sieved

A

if droplet stage was sieved it would go right through and it was dried it would turn into a flat cake

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10
Q

Nature and extent of liquid bridges

A
  • Formation of liquid bridges between particles of powder
  • Nature and extent of liquid bridges dependant on amount of liquid added and method of wet massing
  • 4 stages of bridge formation
  • Agglomerates constantly formed and destroyed
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11
Q

Mechanism of particle-bonding with granulating fluid

A
  • In dry methods particle adhesion takes place due to pressure
  • In wet granulation particles adhere because of liquid
  • Precise mechanism of powder to granule formation different for all equipment.
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12
Q

Mechanism of particle-bonding with granulating fluid - In general 3 phases of agglomeration occur

A

– Nucleation
– Transition
– Ball growth

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13
Q

Phases of agglomeration

A

• Nucleation
– Particle-particle contact and formation of liquid bridges
– Further agitation densifies pendular state which acts as a nuclei for further granule growth
• Transition
– Nuclei can grow by single particles being added via pendular bridges or two or more nuclei can combine
– Wide size distribution exhibited
• Ball growth
– Further granule growth produces large, spherical granules with size
increasing over time.
– Agitation stopped (would promote further coalescence making over- massed particles)

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14
Q

Formation of solid bridges

A

• Partial melting
– Pressures used in dry granulation may cause melting of low melting point materials ( as mp decreases, pressure increases)
– Crystallisation of the materials helps bond the particles together when the pressure is relieved
• Hardening binders
– Binders used in granulating fluid harden or crystallise on drying
– Synthetic polymers and pre-gelatinised starch
• Crysallisation of dissolved materials
– Some of the powders in the mix may be soluble
and dissolved in the granulating liquid
– Crystallisation of the dissolved substances may happen when the granules are dried eg. Lactose
– Slower drying times result in larger crystals

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15
Q

Advantages and disadvantages of wet granulation (most used for tablets, good for forming hard and less brittle tablets due to binding agent)

A

• Advantages
– Reduced segregation of formulation components during
storage/processing
– Useful for formulation of tablets with low active ingredient concentrations
– Uses conventional excipients
– Can be post-processed (tablet coating - enteric coating will allow dissolution of the tablet to occur in the small intestine instead of the stomach as its more acidic)

• Disadvantages
– Several processing steps needed
– Solvents used in process lead to concerns i.e. stability of drugs, toxicology of formulation

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16
Q

Dry granulation (widely used but not as popular as wet granulation as higher pressures and more machinery needed in dry granulation)

A

• No liquids
• Suitable for formulation where:
– Product is moisture sensitive
– Drug is heat sensitive
– Poor compression exhibited after wet granulation
• Aggregation of primary powder particles to form granules and subsequently tablets under high pressure
– Compression of dry powders
– Mill used to break up compacts / ‘slug’ into granules

17
Q

• Slugging

A

– Process used to compress dry powders into a large
‘oversized’ tablet (slug)
– Around 25 mm in diameter, 10-15 mm thickness
– Large heavy duty tablet press used (dangerous)
– Binder can be used to improve bonding strength in compaction
– Disintegrant can be used as excipient (disintegrants are put into the tablet mix and are bound to swell when they hit the liquid in GI tract)
– Lubricant can be added to prevent compacts sticking to the punches and die

18
Q

• Roller compaction

A

– Dry powder mix squeezed between two rollers to
form compressed sheet
– Brittle sheet immediately broken into flakes or milled into correct size
– Flakes ͢ granules
– Can be compacted with binder to improve
bonding strength
– Roller compaction required less lubricant than for slugging (constant movement through a sheet and not hard pressure)

19
Q

Types of excipients

A

• Diluent (filler) e.g. lactose, starch
– Bulks up powder mix
• Disintegrant e.g.starch, sodium starch glycolate
– To break up granule / tablet in solution
– Not the same as dissolution
• Binders
– Bind constituents together
• Lubricant e.g. stearates, PEG, SDS
• Glidant e.g. talc, colloidal silicone dioxide
– Anti-adherent properties

20
Q

Advantages and disadvantages of dry granulation

A

• Advantages
- Less wastage than wet granulation
– Both roller compaction and slugging require conventional
excipients
– Methods not commonly associated with degradation/alteration of drug molecules during processing
– No heat or solvents required
• Disadvantages
– Roller compaction requires specialist equipment
– Segregation of components may occur post processing
– May be issues regarding powder flow
– Final tablets usually softer than with wet granulation
- Cannot be used for EC tabs

21
Q

Wet granulators - 3

A
  • Low shear mixers
  • High-speed granulators
  • Fluidised-bed granulators
22
Q

Granulating agents (usually polymers)

A
• Hydroxylpropyl methylcellulose (HPMC) 2-8% – Various MW and viscosities available
– Soluble in water and ethanol
• Methylcellulose (MC) 1-5%
– Low viscosity grades commonly used
• Starch5-25%
– Requires preparation as a paste
• Pre-gelatinised starch 5-10% 
– Easier to prepare than starch
• Acacia 1-5%
– Requires preparation as a paste
– Can result in prolonged disintegration times at high concentrations
• Polyvinylpyreolidone (PVP) 2-8%
– Various MW and viscosities available 
– Dry or in solution
– Soluble in water and ethanol
23
Q

What properties would be desirable in a granulating fluid?

A

dries at a relatively low boiling point
non-toxic
cheap
upon drying be able to hold crystals together

24
Q

How does the volume of granulating fluid affect formation of granules?

A

if you exceed the amount of granulation fluid, particles will never sieve or dry

25
Q

Spheronisation

A

• Form of granulation
• Makes uniform sized spherical pellets
• Used when spheres required as dosage form
• Useful for M/R or C/R formulations
– Coating is possible
– Multiparticulate systems
• More labour intensive than other forms of granulation – Only used when other forms inappropriate
• Wet massing important to produce good quality spheres
– Usually higher fluid volumes than in wet granulation

26
Q

Transition from rod-shaped to spherical particles

A
  • Cylinder
  • Cylinder with rounded ends
  • Dumbbell
  • Ellipsoid
  • Sphere
  • Water level is critical for optimising the spheronisation process - if you increase water the edges of the cylinder become rounder
27
Q

Types of extruders

A
  • screw feed
  • gravity feed
  • piston feed