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Freeze-drying Critical
Temperatures
Why are Critical Temperatures
important in freeze-drying?
• Freeze-drying above the         • Freeze-drying too far
  product critical                  below the product critical
  temperature can lead to:          temperature can led to:
   – Loss of physical structure      – Poor efficiency
   – Incomplete drying (high         – High running costs
     moisture content)               – Longer cycles than
   – Decreased solubility              necessary
   – Reduced activity and/or
     stability
Critical Temperatures for freeze-
drying
• Collapse Temperature (Tc)
  – This is the temperature at which the material softens
    to the point of not being able to support its own
    structure
• Eutectic Temperature (Teu)
  – This is the temperature at which the solute material
    melts, preventing any structure from forming after the
    solvent has been removed
• All formulations can be described as having
  either a Collapse or a Eutectic Temprature.
Effect on formulation components on
critical temperature
• Higher molecular weight components such as polymers
  tend to have higher critical temperatures
• Lower molecular weight components such as salts and
  small sugars tend to have lower critical temperatures
• Additionally, crystalline/amorphous mix can have a major
  impact on critical temperature:
   – Lactose + NaCl (1:1)     Tc ≈ -30 C
   – Lactose + NaCl (1:0.3)   Tc ≈ -45 C
Critical Temperature
Determination
• Using extensive knowledge and experience in
  the freeze-drying industry, BTL has developed
  two unique analytical instruments. These bring
  scientific understanding and a rational approach
  to freeze-drying cycle development:




             Lyostat3                  Lyotherm2
     Freeze-drying microscope   DTA & Impedance Analyser
Lyostat3 – Freeze-drying
microscope
• Enables real-time observation of the behaviour of your
  formulation during freeze-drying
• Enables temperature control between -196 C and 125 C
  to an accuracy of 0.1 C
• By observing the sample structure during drying as the
  temperature is raised, the exact point of collapse or
  eutectic melt can be observed under the microscope.
Lyotherm2 – DTA and
Impedance Analyser
• Provides and integrated Differential Thermal Analyser
  (DTA) and Electrical Impedance Analyser (zsinφ)
  capability in one instrument
• Can measure critical events in the frozen material that
  are undetectable by standard thermal analysis
  techniques
• Enables characterisation of the required freezing
  parameters that are essential to a successful freeze-
  drying cycle
Critical Temperature Application
   Cycle Development

• From analysis of the product we can determine:
  – The maximum product temperature we can freeze-dry
    at before the product is damaged, allowing us to set
    the primary drying temperature with confidence – by
    Lyostat3 analysis
  – What events occur in the frozen state that affect the
    freezing stage of the cycle, allowing us to add in any
    thermal treatment steps such as annealing – by
    Lyotherm2 analysis
Case Study
   Product Cycle Development

• A customer approached BTL with a product that
  was being freeze-dried using a cycle borrowed
  from another product
• They were discarding a high percentage of each
  batch due to defects occurring during freeze-
  drying
Case Study
   Product Cycle Development

1. Information was obtained on the critical temperatures
   and thermal behaviour of the product using Lyostat3
   and Lyotherm2
2. This data confirmed the lack of suitability of the existing
   freeze-drying cycle
3. Critical temperature information was used to create a
   ‘first approximation’ cycle, tailored to the needs of the
   product.
4. Date from this cycle was used to design a more
   optimised cycle until a safe and efficient cycle was
   achieved, minimising cycle time without jeopardising
   product quality
Case Study
    Lyostat3 analysis

Sample dries well at -50 C, but collapse
  starts as the temperature is increased
  to -45.7 C. This can be identified by
  defects appearing in the dried
  material


As the temperature increases to -39.6 C
  the structure continues to weaken and
  collapse becomes more evident
Case Study
    Lyostat3 analysis

The analysis is repeated but with an
  added heat annealing step – frozen to
  -50 C, warmed to -15 C and cooled
  back to -50 C. Defects don’t appear
  until -31.4 C upon drying


As the temperature increases to -30.8 C
  the structure continues to weaken and
  collapse becomes more evident
Case Study
  Lyotherm2 analysis




                       1
                           2
                               3


                                   4
Case Study
   Lyotherm2 analysis

1. Exotherm in DTA and increase in Impedance
   indicating a stabilisation/rearrangement of the
   frozen structure
2. Increase in downwards gradient of Impedance
   curve indicating a softening of the frozen
   material
3. Onset of a sharp endotherm consistent with the
   melting of the ice
4. Minimum Impedance indicating complete
   mobility within the solute structure
Case Study
   Interpretation of analytical results

• From the results of these analyses, we can me
  the following deductions:
  – The inclusion of an annealing step resulted in an
    increase in the collapse temperature from -45.7 C to
    -31.4 C, as well as increasing the ice crystal size and
    networking
  – Therefore, the maximum allowable product
    temperature during sublimation (to avoid collapse)
    was raised by 14.3 C by annealing, thereby allowing
    drying at higher temperatures, for a more efficient
    cycle. The higher the product temperature, the faster
    the drying rate
Case Study
    Existing customer cycle – 70 hours



              1                   2                            3


+20 C                                 A


-15 C

-40 C                                                                         Tc = -45.7 C
-50 C

               Shelf                        Product                Chamber
            Temperature                   Temperature              Pressure
                  1 – Freezing 2 – Primary Drying 3 – Secondary Drying

                             A – Product at risk of collapse
Case Study
    BTL cycle – 42 hours (including annealing)



         1       2              3                       4


+20 C


-15 C
                                                                          Tc = -31.4 C
-35 C
-50 C


                Shelf                    Product               Chamber
             Temperature               Temperature             Pressure

         1 – Freezing 2 – Annealing 3 – Primary Drying 4 – Secondary Drying
Case Study
    Enlarged section of previous graph




                                        3


+20 C                       The Sublimation Cooling Effect
                      The lowering of product temperature caused
                               by the sublimation of ice
-15 C
                                                                              Tc = -31.4 C
-35 C
-50 C


               Shelf                     Product                   Chamber
            Temperature                Temperature                 Pressure

         1 – Freezing 2 – Annealing 3 – Primary Drying 4 – Secondary Drying
Case Study
  The next steps

• From the previous run, we now know:
  – The extent of sublimation cooling, allowing us to
    increase the shelf temperature & chamber pressure
    as high as possible whilst sublimation cooling keep
    the product temperature below Tc
  – When sublimation was complete in temperature
    probed samples
  – The physical appearance of the cakes produced by
    the cycle
  – Residual moisture was measured in the final product,
    in order to establish whether the extent of secondary
    drying was sufficient
Case Study
   End results

• A freeze-drying cycle with increased efficiency,
  reduced costs and no product rejects

• Another very happy customer!
What is BTL?
• Biopharma Technology Ltd was set up in 1997 to provide
  an international service in all aspects of freeze-drying
  technology.
• Our strength comes from a wealth of experience and
  knowledge of product formulation and process
  development, particularly in the field of pharmaceuticals
  and biotechnology.
Biopharma House, Winnall Valley Road, Winchester SO23 0LD, UK
Tel: +44 (0)1962 841092             Web: www.btl-solutions.net

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The Importance of Critical Temperatures in the Freeze Drying of Pharmaceuticals

  • 2. Why are Critical Temperatures important in freeze-drying? • Freeze-drying above the • Freeze-drying too far product critical below the product critical temperature can lead to: temperature can led to: – Loss of physical structure – Poor efficiency – Incomplete drying (high – High running costs moisture content) – Longer cycles than – Decreased solubility necessary – Reduced activity and/or stability
  • 3. Critical Temperatures for freeze- drying • Collapse Temperature (Tc) – This is the temperature at which the material softens to the point of not being able to support its own structure • Eutectic Temperature (Teu) – This is the temperature at which the solute material melts, preventing any structure from forming after the solvent has been removed • All formulations can be described as having either a Collapse or a Eutectic Temprature.
  • 4. Effect on formulation components on critical temperature • Higher molecular weight components such as polymers tend to have higher critical temperatures • Lower molecular weight components such as salts and small sugars tend to have lower critical temperatures • Additionally, crystalline/amorphous mix can have a major impact on critical temperature: – Lactose + NaCl (1:1) Tc ≈ -30 C – Lactose + NaCl (1:0.3) Tc ≈ -45 C
  • 5. Critical Temperature Determination • Using extensive knowledge and experience in the freeze-drying industry, BTL has developed two unique analytical instruments. These bring scientific understanding and a rational approach to freeze-drying cycle development: Lyostat3 Lyotherm2 Freeze-drying microscope DTA & Impedance Analyser
  • 6. Lyostat3 – Freeze-drying microscope • Enables real-time observation of the behaviour of your formulation during freeze-drying • Enables temperature control between -196 C and 125 C to an accuracy of 0.1 C • By observing the sample structure during drying as the temperature is raised, the exact point of collapse or eutectic melt can be observed under the microscope.
  • 7. Lyotherm2 – DTA and Impedance Analyser • Provides and integrated Differential Thermal Analyser (DTA) and Electrical Impedance Analyser (zsinφ) capability in one instrument • Can measure critical events in the frozen material that are undetectable by standard thermal analysis techniques • Enables characterisation of the required freezing parameters that are essential to a successful freeze- drying cycle
  • 8. Critical Temperature Application Cycle Development • From analysis of the product we can determine: – The maximum product temperature we can freeze-dry at before the product is damaged, allowing us to set the primary drying temperature with confidence – by Lyostat3 analysis – What events occur in the frozen state that affect the freezing stage of the cycle, allowing us to add in any thermal treatment steps such as annealing – by Lyotherm2 analysis
  • 9. Case Study Product Cycle Development • A customer approached BTL with a product that was being freeze-dried using a cycle borrowed from another product • They were discarding a high percentage of each batch due to defects occurring during freeze- drying
  • 10. Case Study Product Cycle Development 1. Information was obtained on the critical temperatures and thermal behaviour of the product using Lyostat3 and Lyotherm2 2. This data confirmed the lack of suitability of the existing freeze-drying cycle 3. Critical temperature information was used to create a ‘first approximation’ cycle, tailored to the needs of the product. 4. Date from this cycle was used to design a more optimised cycle until a safe and efficient cycle was achieved, minimising cycle time without jeopardising product quality
  • 11. Case Study Lyostat3 analysis Sample dries well at -50 C, but collapse starts as the temperature is increased to -45.7 C. This can be identified by defects appearing in the dried material As the temperature increases to -39.6 C the structure continues to weaken and collapse becomes more evident
  • 12. Case Study Lyostat3 analysis The analysis is repeated but with an added heat annealing step – frozen to -50 C, warmed to -15 C and cooled back to -50 C. Defects don’t appear until -31.4 C upon drying As the temperature increases to -30.8 C the structure continues to weaken and collapse becomes more evident
  • 13. Case Study Lyotherm2 analysis 1 2 3 4
  • 14. Case Study Lyotherm2 analysis 1. Exotherm in DTA and increase in Impedance indicating a stabilisation/rearrangement of the frozen structure 2. Increase in downwards gradient of Impedance curve indicating a softening of the frozen material 3. Onset of a sharp endotherm consistent with the melting of the ice 4. Minimum Impedance indicating complete mobility within the solute structure
  • 15. Case Study Interpretation of analytical results • From the results of these analyses, we can me the following deductions: – The inclusion of an annealing step resulted in an increase in the collapse temperature from -45.7 C to -31.4 C, as well as increasing the ice crystal size and networking – Therefore, the maximum allowable product temperature during sublimation (to avoid collapse) was raised by 14.3 C by annealing, thereby allowing drying at higher temperatures, for a more efficient cycle. The higher the product temperature, the faster the drying rate
  • 16. Case Study Existing customer cycle – 70 hours 1 2 3 +20 C A -15 C -40 C Tc = -45.7 C -50 C Shelf Product Chamber Temperature Temperature Pressure 1 – Freezing 2 – Primary Drying 3 – Secondary Drying A – Product at risk of collapse
  • 17. Case Study BTL cycle – 42 hours (including annealing) 1 2 3 4 +20 C -15 C Tc = -31.4 C -35 C -50 C Shelf Product Chamber Temperature Temperature Pressure 1 – Freezing 2 – Annealing 3 – Primary Drying 4 – Secondary Drying
  • 18. Case Study Enlarged section of previous graph 3 +20 C The Sublimation Cooling Effect The lowering of product temperature caused by the sublimation of ice -15 C Tc = -31.4 C -35 C -50 C Shelf Product Chamber Temperature Temperature Pressure 1 – Freezing 2 – Annealing 3 – Primary Drying 4 – Secondary Drying
  • 19. Case Study The next steps • From the previous run, we now know: – The extent of sublimation cooling, allowing us to increase the shelf temperature & chamber pressure as high as possible whilst sublimation cooling keep the product temperature below Tc – When sublimation was complete in temperature probed samples – The physical appearance of the cakes produced by the cycle – Residual moisture was measured in the final product, in order to establish whether the extent of secondary drying was sufficient
  • 20. Case Study End results • A freeze-drying cycle with increased efficiency, reduced costs and no product rejects • Another very happy customer!
  • 21. What is BTL? • Biopharma Technology Ltd was set up in 1997 to provide an international service in all aspects of freeze-drying technology. • Our strength comes from a wealth of experience and knowledge of product formulation and process development, particularly in the field of pharmaceuticals and biotechnology.
  • 22. Biopharma House, Winnall Valley Road, Winchester SO23 0LD, UK Tel: +44 (0)1962 841092 Web: www.btl-solutions.net