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INTRODUCTION
Decreasing the timeframe for cell culture process development has been a key goal towards accelerating biopharmaceutical development.
Automated Micro-scale Bioreactors (ambr™) is an advanced micro bioreactor system with miniature single-use bioreactors with a 9-15mL
working volume controlled by an automated workstation. This system was compared to conventional bioreactor systems in terms of its
performance for the production of a monoclonal antibody and a non-antibody molecule in recombinant Chinese Hamster Ovary (CHO) cell
lines.
The miniaturized bioreactor system was found to produce cell culture profiles that matched across scales to 3L, 15L and 200L stirred tank
bioreactors. Moreover, changes to important process parameters in ambr™ resulted in predictable cell growth, viability and titer changes, which
were in good agreement to historical data from the larger scales. ambr™ was found to successfully reproduce variations in temperature, dissolved
oxygen and pH conditions similar to the larger bioreactor systems. Additionally, the miniature bioreactors were found to react well to
perturbations in pH and dissolved oxygen through adjustments to the PID control loop. Overall, the studies demonstrate the utility of the
ambr™ system as a high throughput system for cell culture process development.
High-throughput Miniaturized Bioreactors for Cell Culture
Process Development: Reproducibility, Scalability and Control.
Shahid Rameez, Sigma S. Mostafa, Anushya Mani, Haiou Yang, Christopher Miller and Abhinav A. Shukla
KBI Biopharma, 1101 Hamlin Road, Durham, NC 27704
ambrTM SYSTEM
ABILITY TO MAKE KEY PROCESS DECISIONS FASTER DURING CELL CULTURE PROCESS
DEVELOPMENT
CASE STUDY I: Reproducibility of key historical results in ambrTM for the production of a monoclonal antibody in a CHO cell line.
 Combination of pH and DO control and an automated liquid handling system in ambrTM system overcomes major
limitations of conventional small-scale cultures vessels especially shake flasks.
 The single-use, pre-calibrated, and instrumented vessels used in ambrTM provides a platform for high-throughput in cell
culture process development while mimicking a stirred-tank bioreactor environment.
Results:
 Both lower pH set-points and Temperature Shift showed higher cell growth, better cell viabilities. DO as suspected had minimal effect on cell
growth and viability.
 Processes at lower pH set-points and with Temperature Shift showed higher cell titers. As observed historically for this process, Temperature
shift was found to be the most important process factor to regulate the productivity of the antibody titer.
 The ambrTM system can be used as a high-throughput platform to make key process decisions during the early process
development phase of biopharmaceutical development.
Time courses for viable cell growth, viability and antibody titer for recombinant CHO cell line with changing (A) Process pH (B) Temperature (C) Dissolved Oxygen (DO)
levels and (D) Feeding Strategies. The experimental data shows an average of 2-3 vessels in the ambrTM system. The error bars show the standard deviation.
The scope of the study was to evaluate if key observations from historical data in other scales bioreactors could be reproduced in ambrTM
system. Some Key Observations from Historical Data were:
 Temperature Shift during the cell culture process was found to be the most important process factor to regulate the productivity of the
antibody.
 The CHO cell line performed better at lower pH set point of 6.85 as compared to pH set point of 7.00
 Feeding intermittently had shown to regulate growth and productivity in the process. Intermittent feeding had showed better results than just
Day 0 additions of feeds.
Based on process knowledge, DO levels (20-50%) were expected to have minimal effect on cell growth and viability.
 Both the case studies (with antibody and a non antibody) demonstrate the utility of the ambr™ system as
a high throughput system for cell culture process development.
Comparison of time courses for viable cell growth and viability for
recombinant CHO cell line in ambrTM and other scales bioreactors:
3, 15L glass bioreactors and 200L disposable bioreactor.
The aim was to compare growth profiles, titer and product quality to other scales 3, 15 and 200L.
Bioreactor System Vendor Maximum Working
Volume (L)
Catalog # / Model
3L Applikon 2.50 Z611000310
15L Applikon 15.00 Z611001510
200L Xcellerex 200.00 888-0151
Table 1: Bioreactors used during the historical cell culture process evaluated in this study.
COMPARISON FOR CELL GROWTH, TITER & PRODUCT QUALITY WITH BIOREACTORS
ACROSS VARIOUS SCALES
CASE STUDY II: Production of a monoclonal antibody in a recombinant CHO cell line in ambrTM and other scales bioreactors
CASE STUDY III: Production of a non-antibody in a recombinant CHO cell line in ambrTM and other scales bioreactors
Comparison of time courses for viable cell growth, viability and titers for recombinant CHO cell line in ambrTM and other scales bioreactors:
15L glass bioreactors and 200L disposable bioreactor.
This protein molecule had two Isomers (A and B). The levels of
Isomers A and B were considered as a product quality attribute.
Results:
Ratio of Isomers A and B were similar (± 5% of mean values)
across ambrTM , 15 and 200L Bioreactors.
Results:
The cell growth and titers within ± 10% of mean values across all scales.
Bioreactor System Cell Maximum Growth Ratee
(1/d)
Cell-specific Productivity
(pg/cell/d)
ambra
0.159 ± 0.001 16.20 ± 0.02
200Lb
0.150 11.70
15Lc
0.150 10.80± 0.02
3Ld
0.162 10.60
Table 2: Cell culture performance comparison between bioreactor systems (ambrTM, 3 and 15L glass
bioreactors and 200L disposable bioreactor) for Cell-maximum growth rate (1/d) and Cell-specific
productivity (pg/cell/d).
ABILITY TO ACCURATELY AND EFFECTIVELY CONTROL pH AND DO DEVIATIONS
The above figure shows schematic of pH control in ambrTM established using the automated liquid handler based base additions
when pH drops below the pH set point. When the pH exceeds the pH set point, the CO2 flow rate increases to establish control
on the pH deviation.
Online profiles for process pH (top left figure) and DO (bottom left figure)
levels during the culture duration for CHO cell line expressing a
recombinant antibody in ambrTM.
The spikes in the DO profiles corresponded to bioreactor sampling, Liquid
additions and Sampling.
All these operations disturb the headspace and alter the working volume.
The time for the DO traces to equilibrate to setpoint after such
manipulations would depend on the controller setup.
CONCLUSION
The multi-stage nature of process development makes it time and resource intensive. A high throughput scale down
approach to upstream process development is needed to decrease the timeframe from DNA to toxicology studies prior to clinical
entry. The results from the study indicate that ambr™ operated under fed-batch conditions with pH, DO and feed control could
successfully simulate bioreactor culture conditions with highly reproducible results between the replicates. Cell growth, process
capabilities, antibody titer and product quality profiles were assessed and compared to historical classical bioreactor cultivations
and found to be within 5-15% of the historical values.
The reproducibility of key results observed in historical process development demonstrated that ambr™ is capable of
providing predictive results under bioreactor relevant process conditions. The 24 single use vessels provide flexibility to run
larger experimental designs at a time to evaluate feeding regimes, process operating limits and interactions between various
operating parameters. The experiments with pH drift control and excursions in process DO set points demonstrated the process
control capability of ambr™. This system offers the realistic possibility of decreasing the process development time for
investigational biopharmaceuticals to reach the clinic.
CASE STUDY IV: Excursions in process pH and DO to test process robustness and failure limits for process
parameters.
Artificial perturbations in pH and DO (by adding a basic feed and changing DO set points respectively) during production of
an antibody molecule in a recombinant CHO cell process. Through adjustments to the PID control loop and gas flow rates
the capability of ambr™ system was evaluated.
Results:
The DO set points were changed to 80% from 20 and
40%, respectively and maintained at 80% for duration of 6 hours.
Afterwards, the DO was changed back to original set points 20
and 40%, at the rate of ≈ 0.5% DO/min based on the tuned
controller set up.
Results:
Tuning the gas flow limits and proportional gains in
the PID loop of ambr™ system; By changing the
proportional gain by eight folds and CO2 gas limits by 1.25
and > 2 folds as opposed to default manufacturer values, the
pH deviation were reduced by 23 and 47 % of initial value,
respectively.
 The capability of inducing deviations can help in designing worst-case experiments for testing process
robustness. It enables to test operating limits with respect to key operational parameters (DO, pH) in a process.
Role of ambr™ in rapid product development throughout the biotech development lifecycle.
a: n = 3, b: n = 1, c: n = 4, d: n = 1.e: Measured from days 0-8.
Titer(mg/mL)
ambr 15L 200L

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High-throughput Miniaturized Bioreactors for Cell Culture Process Development: Reproducibility, Scalability and Control.

  • 1. INTRODUCTION Decreasing the timeframe for cell culture process development has been a key goal towards accelerating biopharmaceutical development. Automated Micro-scale Bioreactors (ambr™) is an advanced micro bioreactor system with miniature single-use bioreactors with a 9-15mL working volume controlled by an automated workstation. This system was compared to conventional bioreactor systems in terms of its performance for the production of a monoclonal antibody and a non-antibody molecule in recombinant Chinese Hamster Ovary (CHO) cell lines. The miniaturized bioreactor system was found to produce cell culture profiles that matched across scales to 3L, 15L and 200L stirred tank bioreactors. Moreover, changes to important process parameters in ambr™ resulted in predictable cell growth, viability and titer changes, which were in good agreement to historical data from the larger scales. ambr™ was found to successfully reproduce variations in temperature, dissolved oxygen and pH conditions similar to the larger bioreactor systems. Additionally, the miniature bioreactors were found to react well to perturbations in pH and dissolved oxygen through adjustments to the PID control loop. Overall, the studies demonstrate the utility of the ambr™ system as a high throughput system for cell culture process development. High-throughput Miniaturized Bioreactors for Cell Culture Process Development: Reproducibility, Scalability and Control. Shahid Rameez, Sigma S. Mostafa, Anushya Mani, Haiou Yang, Christopher Miller and Abhinav A. Shukla KBI Biopharma, 1101 Hamlin Road, Durham, NC 27704 ambrTM SYSTEM ABILITY TO MAKE KEY PROCESS DECISIONS FASTER DURING CELL CULTURE PROCESS DEVELOPMENT CASE STUDY I: Reproducibility of key historical results in ambrTM for the production of a monoclonal antibody in a CHO cell line.  Combination of pH and DO control and an automated liquid handling system in ambrTM system overcomes major limitations of conventional small-scale cultures vessels especially shake flasks.  The single-use, pre-calibrated, and instrumented vessels used in ambrTM provides a platform for high-throughput in cell culture process development while mimicking a stirred-tank bioreactor environment. Results:  Both lower pH set-points and Temperature Shift showed higher cell growth, better cell viabilities. DO as suspected had minimal effect on cell growth and viability.  Processes at lower pH set-points and with Temperature Shift showed higher cell titers. As observed historically for this process, Temperature shift was found to be the most important process factor to regulate the productivity of the antibody titer.  The ambrTM system can be used as a high-throughput platform to make key process decisions during the early process development phase of biopharmaceutical development. Time courses for viable cell growth, viability and antibody titer for recombinant CHO cell line with changing (A) Process pH (B) Temperature (C) Dissolved Oxygen (DO) levels and (D) Feeding Strategies. The experimental data shows an average of 2-3 vessels in the ambrTM system. The error bars show the standard deviation. The scope of the study was to evaluate if key observations from historical data in other scales bioreactors could be reproduced in ambrTM system. Some Key Observations from Historical Data were:  Temperature Shift during the cell culture process was found to be the most important process factor to regulate the productivity of the antibody.  The CHO cell line performed better at lower pH set point of 6.85 as compared to pH set point of 7.00  Feeding intermittently had shown to regulate growth and productivity in the process. Intermittent feeding had showed better results than just Day 0 additions of feeds. Based on process knowledge, DO levels (20-50%) were expected to have minimal effect on cell growth and viability.  Both the case studies (with antibody and a non antibody) demonstrate the utility of the ambr™ system as a high throughput system for cell culture process development. Comparison of time courses for viable cell growth and viability for recombinant CHO cell line in ambrTM and other scales bioreactors: 3, 15L glass bioreactors and 200L disposable bioreactor. The aim was to compare growth profiles, titer and product quality to other scales 3, 15 and 200L. Bioreactor System Vendor Maximum Working Volume (L) Catalog # / Model 3L Applikon 2.50 Z611000310 15L Applikon 15.00 Z611001510 200L Xcellerex 200.00 888-0151 Table 1: Bioreactors used during the historical cell culture process evaluated in this study. COMPARISON FOR CELL GROWTH, TITER & PRODUCT QUALITY WITH BIOREACTORS ACROSS VARIOUS SCALES CASE STUDY II: Production of a monoclonal antibody in a recombinant CHO cell line in ambrTM and other scales bioreactors CASE STUDY III: Production of a non-antibody in a recombinant CHO cell line in ambrTM and other scales bioreactors Comparison of time courses for viable cell growth, viability and titers for recombinant CHO cell line in ambrTM and other scales bioreactors: 15L glass bioreactors and 200L disposable bioreactor. This protein molecule had two Isomers (A and B). The levels of Isomers A and B were considered as a product quality attribute. Results: Ratio of Isomers A and B were similar (± 5% of mean values) across ambrTM , 15 and 200L Bioreactors. Results: The cell growth and titers within ± 10% of mean values across all scales. Bioreactor System Cell Maximum Growth Ratee (1/d) Cell-specific Productivity (pg/cell/d) ambra 0.159 ± 0.001 16.20 ± 0.02 200Lb 0.150 11.70 15Lc 0.150 10.80± 0.02 3Ld 0.162 10.60 Table 2: Cell culture performance comparison between bioreactor systems (ambrTM, 3 and 15L glass bioreactors and 200L disposable bioreactor) for Cell-maximum growth rate (1/d) and Cell-specific productivity (pg/cell/d). ABILITY TO ACCURATELY AND EFFECTIVELY CONTROL pH AND DO DEVIATIONS The above figure shows schematic of pH control in ambrTM established using the automated liquid handler based base additions when pH drops below the pH set point. When the pH exceeds the pH set point, the CO2 flow rate increases to establish control on the pH deviation. Online profiles for process pH (top left figure) and DO (bottom left figure) levels during the culture duration for CHO cell line expressing a recombinant antibody in ambrTM. The spikes in the DO profiles corresponded to bioreactor sampling, Liquid additions and Sampling. All these operations disturb the headspace and alter the working volume. The time for the DO traces to equilibrate to setpoint after such manipulations would depend on the controller setup. CONCLUSION The multi-stage nature of process development makes it time and resource intensive. A high throughput scale down approach to upstream process development is needed to decrease the timeframe from DNA to toxicology studies prior to clinical entry. The results from the study indicate that ambr™ operated under fed-batch conditions with pH, DO and feed control could successfully simulate bioreactor culture conditions with highly reproducible results between the replicates. Cell growth, process capabilities, antibody titer and product quality profiles were assessed and compared to historical classical bioreactor cultivations and found to be within 5-15% of the historical values. The reproducibility of key results observed in historical process development demonstrated that ambr™ is capable of providing predictive results under bioreactor relevant process conditions. The 24 single use vessels provide flexibility to run larger experimental designs at a time to evaluate feeding regimes, process operating limits and interactions between various operating parameters. The experiments with pH drift control and excursions in process DO set points demonstrated the process control capability of ambr™. This system offers the realistic possibility of decreasing the process development time for investigational biopharmaceuticals to reach the clinic. CASE STUDY IV: Excursions in process pH and DO to test process robustness and failure limits for process parameters. Artificial perturbations in pH and DO (by adding a basic feed and changing DO set points respectively) during production of an antibody molecule in a recombinant CHO cell process. Through adjustments to the PID control loop and gas flow rates the capability of ambr™ system was evaluated. Results: The DO set points were changed to 80% from 20 and 40%, respectively and maintained at 80% for duration of 6 hours. Afterwards, the DO was changed back to original set points 20 and 40%, at the rate of ≈ 0.5% DO/min based on the tuned controller set up. Results: Tuning the gas flow limits and proportional gains in the PID loop of ambr™ system; By changing the proportional gain by eight folds and CO2 gas limits by 1.25 and > 2 folds as opposed to default manufacturer values, the pH deviation were reduced by 23 and 47 % of initial value, respectively.  The capability of inducing deviations can help in designing worst-case experiments for testing process robustness. It enables to test operating limits with respect to key operational parameters (DO, pH) in a process. Role of ambr™ in rapid product development throughout the biotech development lifecycle. a: n = 3, b: n = 1, c: n = 4, d: n = 1.e: Measured from days 0-8. Titer(mg/mL) ambr 15L 200L