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The Importance of Understanding the
Physical State of Excipients in a Freeze-
Dried Formulation: Implications for Overall
Product Quality
Juan Davagnino, Ph.D.
Biopharmaceutical Development
KBI Biopharma, Inc.
Lyophilized Formulation Development
• Necessary for products susceptible to storage-induced
physical and chemical degradation
• Removal of water reduces mobility and eliminates
water as a reactant
• Typically necessary to include the following:
• Buffer (minimal)
• Bulking agent
• Stabilizer
• API
• Should minimize total solids (<10% w/v) content in
order to minimize resistance to mass transfer during
drying
Common Lyo Components and
Physical State
• Crystalline
• Bulking agent – mannitol, glycine
• Salt – NaCl, buffer salt in high enough concentrations
• PEG
• Amorphous
• Saccharides – sucrose, trehalose, lactose, etc.
• Polymers – dextran, PVP, etc.
• API – protein, peptide
• Plasticizers (i.e. sorbitol) and Tg modifiers (i.e. HES)
• Buffer salts – diluted into amorphous phase remain
amorphous
The Lyo Process – Impact on Phase
Behavior
• Low temperatures
• Nucleation and growth of ice results in concentration
of solute
• Annealing during freezing may allow for phase
separation in concentrated state
• Annealing allows for crystallization of crystalline
bulking agents, i.e. mannitol, glycine
• Crystallization of excipients can occur during freezing
or early in primary drying
• Crystallization of salts can occur – potential for pH
shift
Potential issues
• Amorphous phase separation may result in separation
of protein and intended stabilizer
• Crystallization of a component intended to remain
amorphous may result in stability and aesthetic
concerns, i.e. cake collapse
• Improper balance of amorphous and crystalline
components may result in delayed or absence of
crystallization
• High amorphous salt concentrations will suppress the
Tg´ making the product more susceptible to collapse
and increase drying times
Case Study: Lyophilized
Formulation Development of an
Enzyme
Formulation Issues on Phase I Product
• Lyophilization cycle needs optimization
• The lyophilized product had to be stored at
-15°C to maintain stability
• Poor lyophilized product appearance
• pH instability at low ionic strength
Client Requirements
• Lyophilized formulation
• Low concentration of enzyme
• Same activity as current formulation (1X PBS)
• High NaCl upon administration
• Need lowest attainable osmolality in lyo product to allow for
recon in NaCl diluent
• Need to study the addition of NaCl in lyo product
• Aesthetically elegant cake
Standard Approach
• Evaluate various formulation buffers, pH, and
excipients
• Narrow down buffer and excipient selections
• Determine ratio of excipients or total excipient
concentration ideal for lyo:
• Ratio of crystalline: amorphous should be at least 3:1
• Total solids should not be less than 3% (w/v)
Formulations Evaluated as part of Study 1
Form. Buffer pH Excipients
A Tris 7.4 3% Mannitol
1% Trehalose
B Tris 7.4 5% Dextran
C Phosphate 7.4 3% Mannitol
1% Trehalose
D Phosphate 7.4 5% Dextran
Lyophilization Cycle – Study 1
-45
-35
-25
-15
-5
5
15
25
35
45
0 5 10 15 20 25 30 35
Time (hours)
Temp
60
70
80
90
100
110
120
Vaccum(mTorrs)
Shelf In
A
B
C
D
Cap Man
Pirani (mTorr)
Sample 
ID  Buffer  pH  Excipient(s) 
A  Tris  7.4  3%(w/v) Mannitol + 1% (w/v) Trehalose 
B  Tris  7.4  5% (w/v) Dextran 
C  Phosphate  7.4  3%(w/v) Mannitol + 1% (w/v) Trehalose 
D  Phosphate  7.4  5% (w/v) Dextran 
Appearance of Cakes
Tr-M/T Ph-M/TTr-D Ph-D
Stability of Enzyme – Post Lyo
Form Buffer Excipients Osm.
(mOsm
/Kg)
NaCl
Added
(mM)
Moisture
(%)
A Tris 3% Mannitol
1% Trehalose
217 40 0.2
B Tris 5% Dextran 24 140 <0.1
C Phosphate 3% Mannitol
1% Trehalose
230 35 0.2
D Phosphate 5% Dextran 30 135 <0.1
Stability of Enzyme – Post Lyo
Sam
ple
Buffer Excipients Assay (%)
A Tris 3% Mannitol
1% Trehalose
84
B Tris 5% Dextran 84
C Phosphate 3% Mannitol
1% Trehalose
143
D Phosphate 5% Dextran 135
Formulations Evaluated as part of Study 2
Sample Buffer pH Excipients
A Tris 7.4 3% Mannitol
1% Trehalose
C Phosphate 7.4 3% Mannitol
1% Trehalose
E Tris 7.4 4% Trehalose
F Phosphate 7.4 4% Trehalose
Lyophilization Cycle – Study 2
-45
-35
-25
-15
-5
5
15
25
35
45
0 5 10 15 20 25 30 35 40 45 50
Time (hours)
Temp
50
55
60
65
70
75
80
85
90
95
100
Vaccum(mTorrs)
Shelf In
A
B
C
Cap Man
Pirani (mTorr)
Appearance of Cakes
Tr-M/T Ph-M/T Ph-TrehTr-Treh
Formulations Evaluated as part of Study 2
Form Buffer Excipients NaCl
(mM)
Assay 1
(%)
A Tris 3% Mannitol
1% Trehalose
40 88
C Phosphate 3% Mannitol
1% Trehalose
30 141
E Tris 4% Trehalose 75 98
F Phosphate 4% Trehalose 70 110
Lyophilization with NaCl – Cycle time
-55
-45
-35
-25
-15
-5
5
15
25
35
45
0 10 20 30 40 50 60 70 80 90 100
Time (hours)
Temp
50
55
60
65
70
75
80
85
90
Vaccum(mTorrs)
Shelf In
A
B
C
Cap Man
Pirani (mTorr)
Lyophilization with NaCl – Cake
Appearance
No impact on appearance when Mannitol is present in
crystalline form!
Addition of NaCl to Trehalose formulation results in
contraction/collapse!
Summary of Lyo Studies
• The Lyo cycle in the
presence of NaCl is too long
and difficult to transfer to a
manufacturing lyophilizer
• The final formulation
contains 10 mM Phosphate,
4% Trehalose pH 7.4 and it
is reconstituted with 70 mM
NaCl to be isotonic.
Conclusions
Initial Product
Development Issues
Improvements Achieved
Lyophilization cycle
needed optimization
The lyophilization cycle was
optimized for the proposed
formulation
The lyophilized product
had to be stored at -15°C
to maintain stability
The product has good stability
at 2-8°C
Poor lyophilized product
appearance
Elegant, homogenous product
appearance
pH instability at low ionic
strength
Stable at isotonic ionic strength

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Importance of Understanding the Physical State of Excipients in a Freeze Dried Formulation

  • 1. The Importance of Understanding the Physical State of Excipients in a Freeze- Dried Formulation: Implications for Overall Product Quality Juan Davagnino, Ph.D. Biopharmaceutical Development KBI Biopharma, Inc.
  • 2. Lyophilized Formulation Development • Necessary for products susceptible to storage-induced physical and chemical degradation • Removal of water reduces mobility and eliminates water as a reactant • Typically necessary to include the following: • Buffer (minimal) • Bulking agent • Stabilizer • API • Should minimize total solids (<10% w/v) content in order to minimize resistance to mass transfer during drying
  • 3. Common Lyo Components and Physical State • Crystalline • Bulking agent – mannitol, glycine • Salt – NaCl, buffer salt in high enough concentrations • PEG • Amorphous • Saccharides – sucrose, trehalose, lactose, etc. • Polymers – dextran, PVP, etc. • API – protein, peptide • Plasticizers (i.e. sorbitol) and Tg modifiers (i.e. HES) • Buffer salts – diluted into amorphous phase remain amorphous
  • 4. The Lyo Process – Impact on Phase Behavior • Low temperatures • Nucleation and growth of ice results in concentration of solute • Annealing during freezing may allow for phase separation in concentrated state • Annealing allows for crystallization of crystalline bulking agents, i.e. mannitol, glycine • Crystallization of excipients can occur during freezing or early in primary drying • Crystallization of salts can occur – potential for pH shift
  • 5. Potential issues • Amorphous phase separation may result in separation of protein and intended stabilizer • Crystallization of a component intended to remain amorphous may result in stability and aesthetic concerns, i.e. cake collapse • Improper balance of amorphous and crystalline components may result in delayed or absence of crystallization • High amorphous salt concentrations will suppress the Tg´ making the product more susceptible to collapse and increase drying times
  • 6. Case Study: Lyophilized Formulation Development of an Enzyme
  • 7. Formulation Issues on Phase I Product • Lyophilization cycle needs optimization • The lyophilized product had to be stored at -15°C to maintain stability • Poor lyophilized product appearance • pH instability at low ionic strength
  • 8. Client Requirements • Lyophilized formulation • Low concentration of enzyme • Same activity as current formulation (1X PBS) • High NaCl upon administration • Need lowest attainable osmolality in lyo product to allow for recon in NaCl diluent • Need to study the addition of NaCl in lyo product • Aesthetically elegant cake
  • 9. Standard Approach • Evaluate various formulation buffers, pH, and excipients • Narrow down buffer and excipient selections • Determine ratio of excipients or total excipient concentration ideal for lyo: • Ratio of crystalline: amorphous should be at least 3:1 • Total solids should not be less than 3% (w/v)
  • 10. Formulations Evaluated as part of Study 1 Form. Buffer pH Excipients A Tris 7.4 3% Mannitol 1% Trehalose B Tris 7.4 5% Dextran C Phosphate 7.4 3% Mannitol 1% Trehalose D Phosphate 7.4 5% Dextran
  • 11. Lyophilization Cycle – Study 1 -45 -35 -25 -15 -5 5 15 25 35 45 0 5 10 15 20 25 30 35 Time (hours) Temp 60 70 80 90 100 110 120 Vaccum(mTorrs) Shelf In A B C D Cap Man Pirani (mTorr) Sample  ID  Buffer  pH  Excipient(s)  A  Tris  7.4  3%(w/v) Mannitol + 1% (w/v) Trehalose  B  Tris  7.4  5% (w/v) Dextran  C  Phosphate  7.4  3%(w/v) Mannitol + 1% (w/v) Trehalose  D  Phosphate  7.4  5% (w/v) Dextran 
  • 12. Appearance of Cakes Tr-M/T Ph-M/TTr-D Ph-D
  • 13. Stability of Enzyme – Post Lyo Form Buffer Excipients Osm. (mOsm /Kg) NaCl Added (mM) Moisture (%) A Tris 3% Mannitol 1% Trehalose 217 40 0.2 B Tris 5% Dextran 24 140 <0.1 C Phosphate 3% Mannitol 1% Trehalose 230 35 0.2 D Phosphate 5% Dextran 30 135 <0.1
  • 14. Stability of Enzyme – Post Lyo Sam ple Buffer Excipients Assay (%) A Tris 3% Mannitol 1% Trehalose 84 B Tris 5% Dextran 84 C Phosphate 3% Mannitol 1% Trehalose 143 D Phosphate 5% Dextran 135
  • 15. Formulations Evaluated as part of Study 2 Sample Buffer pH Excipients A Tris 7.4 3% Mannitol 1% Trehalose C Phosphate 7.4 3% Mannitol 1% Trehalose E Tris 7.4 4% Trehalose F Phosphate 7.4 4% Trehalose
  • 16. Lyophilization Cycle – Study 2 -45 -35 -25 -15 -5 5 15 25 35 45 0 5 10 15 20 25 30 35 40 45 50 Time (hours) Temp 50 55 60 65 70 75 80 85 90 95 100 Vaccum(mTorrs) Shelf In A B C Cap Man Pirani (mTorr)
  • 17. Appearance of Cakes Tr-M/T Ph-M/T Ph-TrehTr-Treh
  • 18. Formulations Evaluated as part of Study 2 Form Buffer Excipients NaCl (mM) Assay 1 (%) A Tris 3% Mannitol 1% Trehalose 40 88 C Phosphate 3% Mannitol 1% Trehalose 30 141 E Tris 4% Trehalose 75 98 F Phosphate 4% Trehalose 70 110
  • 19. Lyophilization with NaCl – Cycle time -55 -45 -35 -25 -15 -5 5 15 25 35 45 0 10 20 30 40 50 60 70 80 90 100 Time (hours) Temp 50 55 60 65 70 75 80 85 90 Vaccum(mTorrs) Shelf In A B C Cap Man Pirani (mTorr)
  • 20. Lyophilization with NaCl – Cake Appearance No impact on appearance when Mannitol is present in crystalline form!
  • 21. Addition of NaCl to Trehalose formulation results in contraction/collapse!
  • 22. Summary of Lyo Studies • The Lyo cycle in the presence of NaCl is too long and difficult to transfer to a manufacturing lyophilizer • The final formulation contains 10 mM Phosphate, 4% Trehalose pH 7.4 and it is reconstituted with 70 mM NaCl to be isotonic.
  • 23. Conclusions Initial Product Development Issues Improvements Achieved Lyophilization cycle needed optimization The lyophilization cycle was optimized for the proposed formulation The lyophilized product had to be stored at -15°C to maintain stability The product has good stability at 2-8°C Poor lyophilized product appearance Elegant, homogenous product appearance pH instability at low ionic strength Stable at isotonic ionic strength