Parallel Integrated Bioreactor Arrays for Bioprocess Development - PowerPoint PPT Presentation

1 / 14
About This Presentation
Title:

Parallel Integrated Bioreactor Arrays for Bioprocess Development

Description:

Parallelism of shake flasks. Automation. Improved data quality. Ease of use ... Similar to Flasks. 6X. 2.4M x 2. Similar to Stirred Tank ... – PowerPoint PPT presentation

Number of Views:58
Avg rating:3.0/5.0
Slides: 15
Provided by: kfje
Category:

less

Transcript and Presenter's Notes

Title: Parallel Integrated Bioreactor Arrays for Bioprocess Development


1
Parallel Integrated Bioreactor Arrays for
Bioprocess Development
  • Harry Lee, Paolo Boccazzi, Rajeev Ram, Anthony
    Sinskey

2
Outline
  • Bioprocesses and bioprocess development
  • Alternative approaches and advantages of
    microfluidics
  • Parallel Integrated Bioreactor Arrays (PIBA)
  • Preliminary biological validation
  • Applications
  • Next steps

3
Bioprocesses
Human insulin
E. coli bacteria
  • Microbial fermentation is used to produce
  • Human insulin, human growth hormone
  • Plasmid DNA vaccine, protein subunit vaccine

Monoclonal antibody
Mammalian cell lines
1000L Bioreactor
  • Mammalian cell culture is used to produce
  • Monoclonal antibodies, Protein therapeutics (ie.
    erythropoietin)
  • Viruses for vaccines

4
Bioprocess development
  • Optimal microbial strains or cell lines must be
    screened
  • Growth conditions must be empirically optimized
  • pH, temperature, nutrients, O2, induction, etc.

Conventional technology
Experimental Throughput
Process Knowledge
5
Properties of ideal system
  • Controlled growth conditions (pH, DO)
  • High oxygen transfer rate
  • Online optical density and growth rate
  • Parallelism of shake flasks
  • Automation
  • Improved data quality
  • Ease of use
  • ? Potential to predict performance
  • in large scale bioreactor

6
Conventional approaches
  • Miniature stirred tanks, enhanced well plates
  • ? Online cell density measurements not reliable
    (bubble interference)
  • ? Measurements require sampling
  • Mechanical multiplexing
  • ? minimal labor savings
  • Robotic multiplexing
  • ? Expensive

7
Microfluidic advantage
  • Microfluidics enables high oxygen transfer rate
    without bubbles
  • Online optical density measurements
  • Online growth rate estimation
  • Integrated sensors and fluidics
  • Measurements do not perturb the fermentation
  • Minimal mechanical parts
  • Compact, bench scale instrument

8
PIBA device module (patent pending)
optical density
Integrated optical oxygen and pH sensors.
(Fluorescence lifetime)

9
E. Coli fermentation in PIBA
45.7
15
30.5
OD 650nm (1cm)
10
Cell density (g-dcw/L)
15.2
5
Similar to Flasks
0
0
  • Highest oxygen transfer rate in mbioreactor array
  • First pH and DO controlled mbioreactor array
  • Growth to cell densities (13g-dcw/L) 4X higher
    than previous mbioreactors
  • Online optical density enabled by bubble free
    oxygenation

7.5
7
pH
6.5
6
120
100
80
DO ( Air Sat)
60
40
20
0
0
1
2
3
4
5
6
7
8
9
Time (h)
10
Unique capability Real time OD monitoring
E. coli growth on LB medium
30
25
20
OD 650nm, 1cm
15
10
5
0
0
1
2
3
4
5
6
7
8
Time (h)
  • Detailed growth kinetics are observable ?
    quantitative study of lag phase
  • Identify nutrient limitations by change in growth
    rate
  • Screening to high cell density is important to
    see nutrient limitations
  • Important to isolate cell density dependent
    phenomena

11
Applications
  • Standard platform for fermentation and cell
    culture
  • Standardization allows sharing data, improved
    data interpretation
  • Standardization was the driver for microfluidics
    in analytics
  • Bioprocess development
  • Improved process optimization
  • Screening based on higher quality data
  • Production scale conditions, growth rate changes
  • Production bioreactor modeling
  • Inhomogeneities, dynamically changing conditions

12
Value Proposition
  • Improved process screening
  • Screen under production scale conditions
  • Early determination of production process yield
  • Impacts investment decision on 500M - 1B
    production facility
  • Production reactor modeling
  • Time varying environment
  • High cell density growth
  • Faster manufacturing scale-up
  • One year shorter time to market for a 500M
    product 30M

13
Next Steps
  • Improved understanding of economic model
  • Case-studies
  • Beta prototype development
  • Improved user friendliness ? fluidic interfaces
  • Improved manufacturing process ? Injection molded
    layers
  • Deploy Beta to collaborators/customers
  • Rigorous biological validation
  • Rank order of process screen the same in PIBA and
    bench scale reactor
  • Production reactor modeling

14
Team
  • Dr. Paolo Boccazzi
  • Microbial Physiology, Molecular Biology,
    Bioprocess Development
  • Dr. Harry Lee
  • Electrical Engineering, Microfabrication, System
    Integration
  • MIT 50K Entrepreneurship Competition Winning
    team member, 2005
  • Prof. Rajeev J. Ram
  • Electrical Engineering, Optoelectronic devices,
    Optical Spectroscopy
  • Director, MIT Center for Integrated Photonic
    Systems
  • Associate Director, Research Laboratory of
    Electronics
  • Prof. Anthony J. Sinskey
  • Biology, Health Sciences and Technology,
    Metabolic Engineering
  • Co-Founder Genzyme, Merrimack Pharmaceuticals,
    Metabolix
Write a Comment
User Comments (0)
About PowerShow.com