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LYOPHILIZATION
TECHNOLOGY
(FREEZE DRYING)
By- SANCHIT
DHANKHAR
Definition
A stabilizing process in which a substance is first
frozen and then the quantity of the solvent is reduced,
first by sublimation (primary drying stage) and then
desorption (secondary drying stage) to values that will
no longer support biological activity or chemical
reactions.
History
Freeze drying was first actively developed during WORLD WAR II transport of
serum.
The main aim was to store the products without refrigeration and to remove
moisture from thermolabile compounds.
 Atlas in 1961 built 6 production freeze drying cabinet for Nestle group in
Germany, Holland.
Principle
 Lyophilization is carried out using a simple principle of physics
sublimation. Sublimation is the transition of a substance from the
solid to the vapour state, without first passing through an
intermediate liquid phase.
 Lyophilization is performed at temperature and pressure
conditions below the triple point, to enable sublimation of ice.
 The entire process is performed at low temperature and pressure
by applying vacuum, hence is suited for drying of thermolabile
compounds.
 The concentration gradient of water vapour between the drying
front and condenser is the driving force for removal of water
during lyophilization.
Objectives of lyophilization process
•To preserve the biological activity of a product.
•To reduce the product weight to lower the transportation cost.
•To extend the shelf life or stability.
•To dry thermolabile materials.
•To eliminate the need for refrigerated storage.
•To get accurate, sterile dosing into the final product container.
Basic components of a Lyophilizer
STEPS INVOLVED IN LYOPHILIZATION
FREEZING STAGE
PRIMARY DRYING STAGE
SECONDARY DRYING STAGE
PACKING
PROCESSING
Fundamental process steps are:
1. Freezing: the product is frozen. This provides a necessary condition
for low temperature
2. Vacuum: after freezing, the product is placed under vacuum. This
enables the frozen solvent in the product to vaporize without passing
through liquid phase, a process known as SUBLIMATION.
3. Heat: Heat is applied to the frozen product to accelerate sublimation.
4. Condensation: Low-temperature condenser plates remove the
vaporized solvent from the vacuum chamber by converting it back to
a solid. This completes the process
LYOPHILIZATION PROCESS
FREEZE DRYING
Freezing the product solution to a temperature below its
eutectic temperature.
Decrease the shelf temperature to -50oc.
Low temperature and low atmospheric pressure are
maintained.
Freons are used as refrigerant.
Formation of ice crystals occurs.
The rate of ice crystallization define the freezing process
and efficiency of primary drying.
PRIMARY DRYING (SUBLIMATION)
Heat is introduced from shelf to the product under graded
control by electrical resistance coils or circulating silicone.
The temperature and pressure should be below the triple point
of water i.e., 0.0098°C and 4.58mmHg.
The driving force is vapor pressure difference between the
evaporating surface and the condenser.
Easily removes moisture up to 98% to 99%.
SECONDARY DRYING (DESORPTION)
The temperature is raised to 50°C – 60°C and vacuum is lowered
about 50mmHg.
Bound water is removed.
Rate of drying is low.
It takes about 10-20 hrs.
LYOPHILIZATION PROCESS
PACKING
• After drying the vacuum is replaced
by filtered dry air or nitrogen to
establish atmospheric pressure
• Ampoules are sealed by either tip
sealing or pull sealing method
• Vials and bottles are sealed with
rubber closures and aluminum caps
FREEZE DRY PRODUCT CHARACTERISTICS
• Sufficient strength
• Uniform color
• Sufficiently dry
• Sufficiently porous
• Sterile
• Free of pyrogens and particulates
• Chemically stable both in dry state and reconstitution
ADVANTAGES OF FREEZE DRYING OVER
CONVENTIONAL DRYING
Product quality Freeze drying Conventional drying
Form of wet material to
be dried
Whole, liquids
Pieces, powders
Pieces
Dry shape and form Maintained Shriveled
Appearance Nearly same Shriveled
color Maintained Faded
Rehydration Fast Slow
Heat exposure 0-150oC 200-300oC
Oxygen exposure Very low High
Retained volatiles Excellent Poor
ADVANTAGES OF LYOPHILIZATION
Removal of water at low temperature
Thermolabile materials can be dried.
Compatible with aseptic operations
More precise fill weight control
Sterility can be maintained.
Reconstitution is easy
DISADVANTAGES OF LYOPHILIZATION
Many biological molecules are damaged by the stress associated
with freezing, freeze-drying, or both.
The product is prone to oxidation, due to high porosity and large
surface area. Therefore the product should be packed in vacuum
or using inert gas or in a container impervious to gases
Cost may be an issue, depending on the product
Long time process
COMMON LYOPHILIZED PRODUCTS
Pharmaceuticals – large and small molecules
Bacteria
Viruses
Vaccines
Plasma
Small zoological specimens
Fruit
Coffee
Flowers
Water-Damaged documents.
APPLICATIONS
Pharmaceutical and biotechnology – to increase the shelf life
of products, such as vaccines and other injectables
Food industry
 to preserve food, very light weight.
 to produce essences or flavouring agents.
 freeze-dried fruits are produced.
 Culinary herbs are preserved.
 Instant coffee powder is prepared.
Technical industries
 in chemical synthesis
Formation of stable products.
Others
 Flora & fauna preservation
 recovery of water-damaged books and documents.
Applications
SOME LYOPHILIZED
FORMULATIONS
Drug Category Route Of
Administration
Marketed Name
Amphotericin B &
Cholestryl sulphate
Anti-fungal IV Infusion at 2-4
mg/kg/hr
Amphotec®
(Sequus
pharmaceuticals)
Chlorthiazide
sodium
Diuretic & anti-
hypertensive
IV Infusion , IV
bolus
Diuril®
(Merck)
Cisplastin Anti-neoplastic IV Infusion,
Platinol®
(Bristol Myers
Oncolgy)
Gemcitabine Anti-neoplastic IV Infusion over 30
min
Genzer®
(Lilly)
Thiopental sodium Short acting
anesthetic IV Infusion
Pentothal sodium®
(Baxter)
Freeze Drying (Lyophilization)- Pharmaceutical Engineering

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Freeze Drying (Lyophilization)- Pharmaceutical Engineering

  • 2.
  • 3. Definition A stabilizing process in which a substance is first frozen and then the quantity of the solvent is reduced, first by sublimation (primary drying stage) and then desorption (secondary drying stage) to values that will no longer support biological activity or chemical reactions.
  • 4. History Freeze drying was first actively developed during WORLD WAR II transport of serum. The main aim was to store the products without refrigeration and to remove moisture from thermolabile compounds.  Atlas in 1961 built 6 production freeze drying cabinet for Nestle group in Germany, Holland.
  • 5. Principle  Lyophilization is carried out using a simple principle of physics sublimation. Sublimation is the transition of a substance from the solid to the vapour state, without first passing through an intermediate liquid phase.  Lyophilization is performed at temperature and pressure conditions below the triple point, to enable sublimation of ice.  The entire process is performed at low temperature and pressure by applying vacuum, hence is suited for drying of thermolabile compounds.  The concentration gradient of water vapour between the drying front and condenser is the driving force for removal of water during lyophilization.
  • 6. Objectives of lyophilization process •To preserve the biological activity of a product. •To reduce the product weight to lower the transportation cost. •To extend the shelf life or stability. •To dry thermolabile materials. •To eliminate the need for refrigerated storage. •To get accurate, sterile dosing into the final product container.
  • 7. Basic components of a Lyophilizer
  • 8. STEPS INVOLVED IN LYOPHILIZATION FREEZING STAGE PRIMARY DRYING STAGE SECONDARY DRYING STAGE PACKING
  • 9. PROCESSING Fundamental process steps are: 1. Freezing: the product is frozen. This provides a necessary condition for low temperature 2. Vacuum: after freezing, the product is placed under vacuum. This enables the frozen solvent in the product to vaporize without passing through liquid phase, a process known as SUBLIMATION. 3. Heat: Heat is applied to the frozen product to accelerate sublimation. 4. Condensation: Low-temperature condenser plates remove the vaporized solvent from the vacuum chamber by converting it back to a solid. This completes the process
  • 11. FREEZE DRYING Freezing the product solution to a temperature below its eutectic temperature. Decrease the shelf temperature to -50oc. Low temperature and low atmospheric pressure are maintained. Freons are used as refrigerant. Formation of ice crystals occurs. The rate of ice crystallization define the freezing process and efficiency of primary drying.
  • 12. PRIMARY DRYING (SUBLIMATION) Heat is introduced from shelf to the product under graded control by electrical resistance coils or circulating silicone. The temperature and pressure should be below the triple point of water i.e., 0.0098°C and 4.58mmHg. The driving force is vapor pressure difference between the evaporating surface and the condenser. Easily removes moisture up to 98% to 99%.
  • 13. SECONDARY DRYING (DESORPTION) The temperature is raised to 50°C – 60°C and vacuum is lowered about 50mmHg. Bound water is removed. Rate of drying is low. It takes about 10-20 hrs.
  • 15. PACKING • After drying the vacuum is replaced by filtered dry air or nitrogen to establish atmospheric pressure • Ampoules are sealed by either tip sealing or pull sealing method • Vials and bottles are sealed with rubber closures and aluminum caps
  • 16. FREEZE DRY PRODUCT CHARACTERISTICS • Sufficient strength • Uniform color • Sufficiently dry • Sufficiently porous • Sterile • Free of pyrogens and particulates • Chemically stable both in dry state and reconstitution
  • 17. ADVANTAGES OF FREEZE DRYING OVER CONVENTIONAL DRYING Product quality Freeze drying Conventional drying Form of wet material to be dried Whole, liquids Pieces, powders Pieces Dry shape and form Maintained Shriveled Appearance Nearly same Shriveled color Maintained Faded Rehydration Fast Slow Heat exposure 0-150oC 200-300oC Oxygen exposure Very low High Retained volatiles Excellent Poor
  • 18. ADVANTAGES OF LYOPHILIZATION Removal of water at low temperature Thermolabile materials can be dried. Compatible with aseptic operations More precise fill weight control Sterility can be maintained. Reconstitution is easy
  • 19. DISADVANTAGES OF LYOPHILIZATION Many biological molecules are damaged by the stress associated with freezing, freeze-drying, or both. The product is prone to oxidation, due to high porosity and large surface area. Therefore the product should be packed in vacuum or using inert gas or in a container impervious to gases Cost may be an issue, depending on the product Long time process
  • 20. COMMON LYOPHILIZED PRODUCTS Pharmaceuticals – large and small molecules Bacteria Viruses Vaccines Plasma Small zoological specimens Fruit Coffee Flowers Water-Damaged documents.
  • 21. APPLICATIONS Pharmaceutical and biotechnology – to increase the shelf life of products, such as vaccines and other injectables Food industry  to preserve food, very light weight.  to produce essences or flavouring agents.  freeze-dried fruits are produced.  Culinary herbs are preserved.  Instant coffee powder is prepared.
  • 22. Technical industries  in chemical synthesis Formation of stable products. Others  Flora & fauna preservation  recovery of water-damaged books and documents. Applications
  • 23. SOME LYOPHILIZED FORMULATIONS Drug Category Route Of Administration Marketed Name Amphotericin B & Cholestryl sulphate Anti-fungal IV Infusion at 2-4 mg/kg/hr Amphotec® (Sequus pharmaceuticals) Chlorthiazide sodium Diuretic & anti- hypertensive IV Infusion , IV bolus Diuril® (Merck) Cisplastin Anti-neoplastic IV Infusion, Platinol® (Bristol Myers Oncolgy) Gemcitabine Anti-neoplastic IV Infusion over 30 min Genzer® (Lilly) Thiopental sodium Short acting anesthetic IV Infusion Pentothal sodium® (Baxter)