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Flexible facility
success
Case study of 12
flexible facility
biopharm projects
Frank Nygaard
May, 2015
2
Content
The 12 projects – common denominators
The 12 projects – the data set
Process design
Facility design and manufacturing strategy - campaign versus concurrent manufacturing
Facility design
Single-use implementation
Capacity expansion strategies
Flexible technology integration
Summary
The 12 projects
Common denominators
3
Single-use technology: Enabler for flexible manufacturing
• Decouples the process from the building
• No complex distribution matrices as connections are flexible
• Media and buffer supply is configured to the given process
• Can start with only 500L bioreactor train and expand rapidly
• 2000L footprint is not drastically larger than 500L footprint
Design basics
• NNE Pharmaplan Bio on demand™ with flexibility as key driver
• Facility designs are for multiproduct manufacturing
• Single-use bioreactors utilised for mammalian fed-batch cell cultivation
• Other process and support systems may be single-use, stainless steel or hybrid systems
The 12 projects
The dataset
4
Basic of design Location
#1 2011 China
#2 2012 Taiwan
#3 2012 Russia
#4 2012 China
#5 2012 Denmark
#6 2013 China
#7 2014 Germany
#8 2014 Brazil
#9 2014 India
#10 2014 Brazil
#11 2015 Malaysia
#12 2015 China
Pilot
(3)
Launch (3)
Commercial
(6)
Manufacturing
scope
Basis for data evaluation
Process design
5
Model processes for design
• “Protein”: 58% (incl. mAbs)
• mAb platform: 42%
Batch size
• Pilot scale SUB: 500 – 1000L
• Launch scale SUB: 1000 – 2000L
• Commercial scale: 2000L 1)
Manufacturing strategy
• Campaign manufacturing: 83%
• Concurrent manufacturing possible: 17% 2)
Facility
Design
Process
design
SUB
size
SUBs
per line
#1 Launch “Protein” 2000L 1x
#2 Pilot “Protein” 500L 2x
#3 Launch mAb 2000L 2x
#4 Commercial mAb 2000L 4x
#5 Pilot “Protein” 1000L 4x
#6 Launch mAb 1000L 2x
#7 Commercial “Protein” 2000L 6x
#8 Commercial mAb 2000L 4x
#9 Commercial “Protein” 2000L 2x
#10 Pilot mAb 1000L 1x
#11 Commercial “Protein” 2000L 2x
#12 Commercial “Protein” 2000L 7x
1) “Scale out” of SUBs to increase batch size included in 29% of commercial designs
2) Concurrent: Manufacturing of different products in cell culture possible at the same time
Facility design and manufacturing strategy
Campaign versus concurrent manufacturing
• Strategic use of manufacturing strategy in the
facility design
• Campaign-based manufacturing
• More upstream lines than downstream
• Concurrent-based manufacturing
• Less upstream lines than downstream
6
Downstream DownstreamUpstream
Downstream
(1 week)
Cell culture
(3 weeks)
DownstreamUpstream Upstream
Facility design
7
Construction design
• 100% stick build (with modular construction evaluated in 17%)
Process design
• 92% traditional design with seed lab, cell culture, initial and final
purification
• 8% “Ballroom” concept (with shared cell culture and purification)
Cleanroom classification
• Seed lab Class C (Iso 7)
• Cell culture Class D (Iso 8)
• Initial purification (pre-virus) Class C (Iso 7) or Class D (Iso 8)
• Final purification (post-virus) Class C (Iso 7)
Single-use implementation
8
Upstream
• Bioreactor: 100%
• Harvest clarification: 66%
• Media preparation: 75%
• Media hold: 92%
Downstream
• Intermediate product hold: 92%
• Process equipment: 17%
• Buffer preparation: 75%
• Buffer hold: 92%
1) SU: Single use chromatography and UF/DF skids not considered
Facility
design
Total
capacity
Technology 1)
#1 Launch 2x 2000L SU
#2 Pilot 2x 500L SU
#3 Launch 2x 2000L SU
#4 Commercial 4x 2000L SU
#5 Pilot 4x 1000L SU
#6 Launch 2x 1000L SU
#7 Commercial 6x 2000L Hybrid
#8 Commercial 12x 2000L SU
#9 Commercial 4x 2000L Hybrid
#10 Launch 1x 1000L SU
#11 Commercial 8x 2000L Hybrid
#12 Commercial 14x 2000L Hybrid
Capacity expansion strategies
9
Equipment
swap
Drop blockFitting out
Capacity expansion strategies
10
• Facility designs with expansion strategy: 92%
• Equipment swap: 25%
• Fitting out: 58%
• Drop block: 17%
• Capacity expansion: 100 - 400%
Equipment
Swap
DropBlock
Fitting Out
Phased expansion Initial
capacity
Final
capacity
#1 Equipment swap 2x 1000L 2x 2000L
#2 Equipment swap 2x 200L 2x 500L
#3 Fitting out 1x 2000L 2x 2000L
#4 Drop block 2x 2000L 4x 2000L
#5 Fitting out 2x 1000L 4x 1000L
#6 Fitting out 1x 500L 2x 1000L
#7 Fitting out 2x 2000L 6x 2000L
#8 Fitting out/Drop block 4x 2000L 12x 2000L
#9 Fitting out 2x 2000L 4x 2000L
#10 Fitting out 1x 500L 1x 1000L
#11 Equipment swap 8x 500L 8x 2000L
#12 14x 2000L 14x 2000L
Flexible technology integration
11
Facility design Perfusion F&F ADC
#1 Launch X
#2 Pilot
#3 Launch
#4 Commercial X
#5 Pilot X
#6 Launch X
#7 Commercial X
#8 Commercial
#9 Commercial X X X
#10 Launch X
#11 Commercial X X
#12 Commercial X
• 83% include a flexible fed-batch facility design:
• Fed-batch to perfusion: 42%
• End-to-end manufacturing (API+F&F): 50%
• Antibody Drug Conjugate (ADC): 8%
Summary
12
• Single-use technology is to key enabler for flexibility
• Hybrid solutions prevalent in the facility designs for commercial production
• “Traditional” layout for upstream and downstream – ballroom design not embraced yet
• Expansion strategy considered in facility designs
• Design for implementation of new technologies
For more information
13
Frank Nygaard
Senior Technology Partner
T: +45 3079 9785
fkny@nnepharmaplan.com
Connect with Frank Nygaard on LinkedIn
Blog by Frank Nygaard: Where does flexibility really matter?:
http://www.nnepharmaplan.com/insights/on-the-move/where-does-flexibility-really-matter/
www.nnepharmaplan.com

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Flexible facility success

  • 1. Flexible facility success Case study of 12 flexible facility biopharm projects Frank Nygaard May, 2015
  • 2. 2 Content The 12 projects – common denominators The 12 projects – the data set Process design Facility design and manufacturing strategy - campaign versus concurrent manufacturing Facility design Single-use implementation Capacity expansion strategies Flexible technology integration Summary
  • 3. The 12 projects Common denominators 3 Single-use technology: Enabler for flexible manufacturing • Decouples the process from the building • No complex distribution matrices as connections are flexible • Media and buffer supply is configured to the given process • Can start with only 500L bioreactor train and expand rapidly • 2000L footprint is not drastically larger than 500L footprint Design basics • NNE Pharmaplan Bio on demand™ with flexibility as key driver • Facility designs are for multiproduct manufacturing • Single-use bioreactors utilised for mammalian fed-batch cell cultivation • Other process and support systems may be single-use, stainless steel or hybrid systems
  • 4. The 12 projects The dataset 4 Basic of design Location #1 2011 China #2 2012 Taiwan #3 2012 Russia #4 2012 China #5 2012 Denmark #6 2013 China #7 2014 Germany #8 2014 Brazil #9 2014 India #10 2014 Brazil #11 2015 Malaysia #12 2015 China Pilot (3) Launch (3) Commercial (6) Manufacturing scope Basis for data evaluation
  • 5. Process design 5 Model processes for design • “Protein”: 58% (incl. mAbs) • mAb platform: 42% Batch size • Pilot scale SUB: 500 – 1000L • Launch scale SUB: 1000 – 2000L • Commercial scale: 2000L 1) Manufacturing strategy • Campaign manufacturing: 83% • Concurrent manufacturing possible: 17% 2) Facility Design Process design SUB size SUBs per line #1 Launch “Protein” 2000L 1x #2 Pilot “Protein” 500L 2x #3 Launch mAb 2000L 2x #4 Commercial mAb 2000L 4x #5 Pilot “Protein” 1000L 4x #6 Launch mAb 1000L 2x #7 Commercial “Protein” 2000L 6x #8 Commercial mAb 2000L 4x #9 Commercial “Protein” 2000L 2x #10 Pilot mAb 1000L 1x #11 Commercial “Protein” 2000L 2x #12 Commercial “Protein” 2000L 7x 1) “Scale out” of SUBs to increase batch size included in 29% of commercial designs 2) Concurrent: Manufacturing of different products in cell culture possible at the same time
  • 6. Facility design and manufacturing strategy Campaign versus concurrent manufacturing • Strategic use of manufacturing strategy in the facility design • Campaign-based manufacturing • More upstream lines than downstream • Concurrent-based manufacturing • Less upstream lines than downstream 6 Downstream DownstreamUpstream Downstream (1 week) Cell culture (3 weeks) DownstreamUpstream Upstream
  • 7. Facility design 7 Construction design • 100% stick build (with modular construction evaluated in 17%) Process design • 92% traditional design with seed lab, cell culture, initial and final purification • 8% “Ballroom” concept (with shared cell culture and purification) Cleanroom classification • Seed lab Class C (Iso 7) • Cell culture Class D (Iso 8) • Initial purification (pre-virus) Class C (Iso 7) or Class D (Iso 8) • Final purification (post-virus) Class C (Iso 7)
  • 8. Single-use implementation 8 Upstream • Bioreactor: 100% • Harvest clarification: 66% • Media preparation: 75% • Media hold: 92% Downstream • Intermediate product hold: 92% • Process equipment: 17% • Buffer preparation: 75% • Buffer hold: 92% 1) SU: Single use chromatography and UF/DF skids not considered Facility design Total capacity Technology 1) #1 Launch 2x 2000L SU #2 Pilot 2x 500L SU #3 Launch 2x 2000L SU #4 Commercial 4x 2000L SU #5 Pilot 4x 1000L SU #6 Launch 2x 1000L SU #7 Commercial 6x 2000L Hybrid #8 Commercial 12x 2000L SU #9 Commercial 4x 2000L Hybrid #10 Launch 1x 1000L SU #11 Commercial 8x 2000L Hybrid #12 Commercial 14x 2000L Hybrid
  • 10. Capacity expansion strategies 10 • Facility designs with expansion strategy: 92% • Equipment swap: 25% • Fitting out: 58% • Drop block: 17% • Capacity expansion: 100 - 400% Equipment Swap DropBlock Fitting Out Phased expansion Initial capacity Final capacity #1 Equipment swap 2x 1000L 2x 2000L #2 Equipment swap 2x 200L 2x 500L #3 Fitting out 1x 2000L 2x 2000L #4 Drop block 2x 2000L 4x 2000L #5 Fitting out 2x 1000L 4x 1000L #6 Fitting out 1x 500L 2x 1000L #7 Fitting out 2x 2000L 6x 2000L #8 Fitting out/Drop block 4x 2000L 12x 2000L #9 Fitting out 2x 2000L 4x 2000L #10 Fitting out 1x 500L 1x 1000L #11 Equipment swap 8x 500L 8x 2000L #12 14x 2000L 14x 2000L
  • 11. Flexible technology integration 11 Facility design Perfusion F&F ADC #1 Launch X #2 Pilot #3 Launch #4 Commercial X #5 Pilot X #6 Launch X #7 Commercial X #8 Commercial #9 Commercial X X X #10 Launch X #11 Commercial X X #12 Commercial X • 83% include a flexible fed-batch facility design: • Fed-batch to perfusion: 42% • End-to-end manufacturing (API+F&F): 50% • Antibody Drug Conjugate (ADC): 8%
  • 12. Summary 12 • Single-use technology is to key enabler for flexibility • Hybrid solutions prevalent in the facility designs for commercial production • “Traditional” layout for upstream and downstream – ballroom design not embraced yet • Expansion strategy considered in facility designs • Design for implementation of new technologies
  • 13. For more information 13 Frank Nygaard Senior Technology Partner T: +45 3079 9785 fkny@nnepharmaplan.com Connect with Frank Nygaard on LinkedIn Blog by Frank Nygaard: Where does flexibility really matter?: http://www.nnepharmaplan.com/insights/on-the-move/where-does-flexibility-really-matter/ www.nnepharmaplan.com