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G. Jyothsna 
256212886012 
M.Pharmacy (Pharmaceutics) 1st yr 
Malla Reddy College Of Pharmacy
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
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.
Applications 
Technical industries 
 in chemical synthesis 
 Formation of stable products. 
 Others 
 Flora & fauna preservation 
 recovery of water-damaged books and documents.
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)
References 
The science and practice of pharmacy by Remington, 21 
edition, vol-1. Pg 828-831. 
The Theory And Practice of Industrial Pharmacy by Leon 
Lachmann, Herbert.A.Lieberman and Joseph I. Kanig, 1991. Pg 
62-64, 672-674. 
Pharmaceutial Engineering – Priniciples and Practices by C.V.S. 
Subramanyam, J. Thimma Setty, Sarasija Suresh and V. Kusum 
Devi. Pg 401-405. 
Aulton’s Pharmaceutics – The Design And Manufacture Of 
Medicines by Micheal E. Aulton, 2009. Pg 195. 
The Lyophilization of Pharmaceuticals: A Literature Review by 
N.A. Williams* and G.P. Polli. Journal of Pharmaceutical 
science and Technology.
Lyophilization

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Lyophilization

  • 1. G. Jyothsna 256212886012 M.Pharmacy (Pharmaceutics) 1st yr Malla Reddy College Of Pharmacy
  • 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. 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. Applications Technical industries  in chemical synthesis  Formation of stable products.  Others  Flora & fauna preservation  recovery of water-damaged books and documents.
  • 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)
  • 24. References The science and practice of pharmacy by Remington, 21 edition, vol-1. Pg 828-831. The Theory And Practice of Industrial Pharmacy by Leon Lachmann, Herbert.A.Lieberman and Joseph I. Kanig, 1991. Pg 62-64, 672-674. Pharmaceutial Engineering – Priniciples and Practices by C.V.S. Subramanyam, J. Thimma Setty, Sarasija Suresh and V. Kusum Devi. Pg 401-405. Aulton’s Pharmaceutics – The Design And Manufacture Of Medicines by Micheal E. Aulton, 2009. Pg 195. The Lyophilization of Pharmaceuticals: A Literature Review by N.A. Williams* and G.P. Polli. Journal of Pharmaceutical science and Technology.