The presentation describes mixing of solid, liquid and semisolid pharmaceutical dosage forms. It includes mechanisms of solid and liquid mixing, interparticle interactions-segregation, factors affecting mixing, applications of mixing and various equipments used for mixing of pharmaceuticals.
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MIXING OF PHARMACEUTICALS.pptx
1. Mixing of Pharmaceuticals
Mr. A.T. Sharma
Assistant Professor
Department of Pharmaceutics
Nanded Pharmacy College, Nanded
2. Mixing
• Definition: A process that tends to result in a
randomization of dissimilar particles within a
system.
• Blending
• Cohesive and Non-cohesive solids
3. Difference Between Solid Mixing and Liquid Mixing
Liquid Mixing
• Flow currents are
responsible for transporting
unmixed material to the
mixing zone adjacent to
impeller.
• Truly homogeneous liquid
phase can be observed.
• Small sample size is
sufficient to study degree of
mixing.
• Mixing requires low power.
Solid Mixing
• Flow currents are not
possible.
• Product often consists of
two or more easily
identifiable phases.
• Large sample is required.
• Mixing requires high power.
4. Applications
• Wet mixing in granulation
• Dry mixing in direct compression
• Dry blending of powders
• Production of pellets
7. Interparticle Interactions - Segregation
• Particle characteristics like size, size distribution,
shape and surface influence the interparticle
interactions in a powder bed.
• Inertial Forces: Tend to hold neighbouring
particles in a fixed relative position.
- van der Waals forces
- Electrostatic forces
- Surface forces
• Gravitational Forces
8. Van der Waals forces
• Weak but general attractive or repulsive forces
between neutral atoms or molecules.
• Differ from covalent or ionic bonding
Electrostatic forces
• The attractive or repulsive force between two
electrically charged objects.
Surface/ Interface forces:
• Cohesive forces – prevent intimate mixing
• Frictional forces – lumps
• Depends on SA, surface roughness, surface polarity,
surface charge, moisture
• For effective mixing, surface to surface interactions
should be minimum – surface treatment
9. Reasons of Segregation
• Poor flow properties of powder bed
• Wide differences in particle sizes
• Differences in mobilities of individual
ingredients
• Differences in particle density and shape
• Transporting stage
• Dusting stage
10. Gravitational Forces
• Tend to improve the movement of two adjacent
particles or groups of particles.
• Tumbling action promotes inter-particulate movement
due to gravitational forces.
• Motion of particles – contact with the mixer surface
or/and from contact with one other
• These motions accelerate translational and rotational
mode of single particle or group of particles
• Particle – particle collisions: Exchange of momentum
• Continuous exchange of momentum between
translational and rotational mode necessary for
effective mixing.
11. Efficiency of momentum transfer depends upon-
• Elasticity of collisions
• Coefficient of friction
• SA of contact
• Surface roughness
• Centrifugal forces
12. Factors Affecting Mixing
• Nature of the surface
• Density of the particles
• Particle size
• Particle shape
• Particle charge
• Proportion of materials
13. Twin Shell Blender/ V Cone Blender
• V shaped shell, stainless steel or transparent plastic
• Small – 20kg/ 35rpm
• Large – 1 tonne/ 15rpm
• Loading – two hatches
• Emptying – apex port
• Material loaded – 50 to 60% of volume
• Rotation - tumbling motion
• V inverted – splitting
• Splitting and dividing repeated
• High speed – dusting/ segregation
• Low speed – poor mixing
14. Double Cone Blender
• Charged and discharged – same port
• Efficient for small amount of powders
• Speed – size, shape of tumbler, nature of
material- 30-100rpm
• Method- same as V cone blender
15. Ribbon Mixer
Principle:
• Shear mixing by ribbon shaped moving blades – breaks
lumps and aggregates
• Convective mixing
Construction:
o Non-movable horizontal cylinder trough open at top
o Two helical blades, same shaft
o Blades with right and left twist – connected to fixed
speed drive
o Top loading, bottom discharge
o Lid at top
16.
17. Sigma Blade Mixer
Principle:
• Shear mixing and kneading actions with sigma
shaped blades
• Convective mixing by cascading
Construction:
o Double trough shaped stationary bowl
o Two sigma shaped blades horizontally fitted
o Fixed speed drive
o Loading from top, unloading by tilting by rack-
and-pinion drive
18.
19. Planetary Mixer
Principle:
• Shear between a moving blade and stationary
wall
• Blade tears mass apart
• Mixing arm moves in two ways, around own
axis and around central axis – no dead spot
• Plates in blade are sloped – powder makes
upward movement - convective mixing
20. Construction
• Vertical cylindrical shell – removable
• Mixing blade at top
• Mixing shaft driven by planetary gear train
with variable speed drive
21. Liquid Mixing
• Formation of homogeneous mass
• Agitation: Induced motion of a material in a
specified way, usually in a circulatory pattern
inside a container
• Mixing: Random distribution into one another
of two or more separate phases
• Applications: Manufacture of emulsions,
suspensions, solutions, aerosols
22. Mechanism of Liquid Mixing
• Bulk transport
• Turbulent mixing
• Laminar mixing
• Molecular diffusion
24. Propellers
• Contains a no. of blades
• Right or left handed
• Deep tank – Push-pull propeller
• Small size
• Speed 8000rpm
• Uses:
- High mixing capacity
- Liquid of maximum viscosity of 2 pascals.second,
slurries
with 10% solids
- Gas-liquid dispersions, multivitamin elixirs, disinfectant
solutions
25.
26. Turbines
• A circular disc with no. of short blades
• Diameter: 30-50%
• Speed: 50-200rpm
• Blades straight, curved, pitched or vertical
• Near the turbine, zone of rapid currents, high
turbulence, and intense shear
• Diffuser ring – stationary, perforated ring
surrounding turbine – reduce swirling and
vortexing
27.
28. Paddles
• A central hub with two long flat vertical
blades
• Pitched, hemispherical with large SA
• A shaft with hub-blades rotates – 100rpm
• Radial and tangential push
• Deep tanks – several blades one above other
• Very low speed – agitation in unbaffled tank
• High speed – baffled tank
31. Silverson Mixer - Emulsifier
Principle:
• Intense shear forces and turbulence by high
speed rotors
• Liquids pass through fine interstices of
perforated metal sheets
• Circulation through head by suction in inlet at
bottom of head
• Rapid breakdown of liquid into smaller
globules
32. Construction:
• Long supporting
columns connected to
motor – support head
• Shaft at centre – one
end to motor, other to
head
• Head has turbine
blades
• Blades surrounded by
a mesh, enclosed by a
cover with openings.
33.
34. Working:
• Head dipped completely in
vessel containing liquids
• Motor started – shaft rotates
head and turbine blades with
very high speed
• Pressure difference created –
liquid sucked from bottom
• Intense mixing
• Centrifugal force expel contents
with great force through mesh
and openings of cover
• Intake and expulsion –
circulation – break down of
globules
Uses: Emulsions and creams of fine
particle size
35. Thank You…!!!
(Disclaimer: The images and diagrams in this
presentation have been downloaded from the google
source. I am grateful to all the publishers & the google.)