SlideShare a Scribd company logo
High throughput bioreactor mimetic in
l d l t t d l tearly and late stage process development
American Chemical Society – Biochemical Technology (BIOT) Division
245th – ACS National Meeting, New Orleans, LA
Shahid Rameez, Ph.D.Shahid Rameez, Ph.D.
Scientist I, Process Development
KBI Biopharma Inc, Durham, NCp
Overview
Ambr System
Bioreactor
Mimetic
In process
Mimetic
KBI Evaluation
p
Activities
&
Design Space
Evaluation
Experimental Design
in Early and Late
C t l St t i
y
Stage Process
Development
Control Strategies
 A key bottleneck in biopharmaceutical development has been they p p
rapid development of robust and scalable manufacturing processes that
can permit accelerated progress of products into clinical trials.
 Innovations in this area can have a very significant impact on the
overall economics of biopharmaceutical drug development by
d i h i i k h h li idecreasing the time it takes to reach the clinic.
 Mammalian cell culture processes typically have the longestp yp y g
experimental duration with 2-3 weeks being a typical duration for the
production bioreactor step with additional time spent on the seed
culturescultures.
 Shake flasks provide the capability to perform high throughput
experiments, but with an inability to control process parameters likeexperiments, but with an inability to control process parameters like
agitation rate, dissolved oxygen (DO) and pH.
 Th t l h l h d l i b t ffi i t These parameters play a huge role when developing a robust, efficient
cell culture process which dictates the product quality and yield.
 Moreover, reproducibility and scalability of process and culture
performance is a pre-requisite for successful and efficient process
development at a scale down level.development at a scale down level.
 At KBI we did case studies evaluating the ambr™ system (an
a tomated micro scale bioreactor s stem) to establish the roleautomated micro-scale bioreactor system) to establish the role
this system could play in accelerating biotech drug development.
Automated Miniaturized Bioreactors
1mL tips
ambrTM Technology
1mL
or
Liquid
Handler
4mL tips
Handler
Used Tips
Discard
Culture stations; each holding 12 bioreactors
ambrTM Deck Layout
Culture stations
1ml tips
4ml tips4ml tips
24 deep-well plate Tip box lid
Plate lid
The Vessel
Vessel Cap:
In-line filter
on gas supply
DO sensor
on gas supply
Impeller
pH sensorp
Culture Station Nomenclature
Culture station 1 (CS1) Culture station 2 (CS2)
CS1-1
CS1-2
CS1-3
CS1-4
CS1-5
CS1-6
Culture station 1 (CS1)
CS2-1
CS2-2
CS2-3
CS2-4
CS2-5
CS2-6
Culture station 2 (CS2)
7
8
9
10
11
12
7
8
9
10
11
12
CS1-7
CS1-8
CS1-9
CS1-1
CS1-1
CS1-1
CS2-7
CS2-8
CS2-9
CS2-1
CS2-1
CS2-1
Id l ki l i 13mL W ki l i 11 15mLIdeal working volume is 13mL; Working volume range is 11 – 15mL
Things to consider:
– Feed strategy and Sampling strategyFeed strategy and Sampling strategy
– Low volumes – gas entrainment / vortexing
– High volumes – Limits kLa.
PART 1:
Reproducibility for Results and Key Observations during Cell Culture Process Development
 The processes evaluated in ambrTM were previously developed from a rigorous
cell culture process development performed in classical bioreactors of various
scales. The process were successfully carried in bioreactors across various scales: 2L,
10L d 200L10L and 200L.
 This study aimed at studying the reproducibility of the key observations of the
processes in ambrTM. Thus a reverse engineering approach was adopted, where we
were cognizant about the outcomes from most of the experiments as far as
inducing process variations was concerned.
 The reproducibility of key historical results in ambrTM would corroborate towards
its capability as a high throughput bioreactor mimetic in cell culture process
development.
K Ob i f Hi i l D
Case Study 1: Reproducibility evaluation for the production of a monoclonal antibody in a
recombinant Chinese Hamster Ovary (CHO) cell line.
Key Observations from Historical Data:
• Temperature Shift during the cell culture process was found to be the most important
process factor to regulate the productivity of the antibody titer.
• 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 for feed.
• A highly basic and a critical feed, referred here as FDX, had to be added without pre-
neutralization with acids to avoid osmolality increase in cultures. Thus, a better control
had to be established in the bioreactors to control the pH drift with addition of FDX.
h h d b b h d hThis was achieved in classical bioreactors by tuning the PID controllers and with
regulation in cascade feedback gassing of CO2 and Air.
Results: Both lower pH set-points and Temperature Shift showed higher cell growth, better
cell viabilities. DO as suspected at negligible effect on cell growth and viability.
Time courses for viable cell growth and viability 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 ambr 24. The error bars show the standard
deviationdeviation.
Results: Both lower pH set-points and 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
bi h i l d lbiopharmaceutical development.
PART B:
Scalability Assessment in Cell Culture Process Development
Case Study 2: Comparison across scales for the production of a monoclonal antibody in a
recombinant CHO cell line.
Ambr (n = 3).
2L (n = 1).
10 ( 4)10L (n = 4).
200L (n = 1).
• Harvest Titers within 1 5 1 7 g/L• Harvest Titers within 1.5 -1.7 g/L
across all scales.
Comparison of time courses for viable cell growth and viability for recombinant CHO cell line in ambrTM and other
scales bioreactors: 2, 10L Glass bioreactors and 200L disposable bioreactor.p
Case Study 3: Comparison across scales for the production of a protein molecule in a
recombinant Chinese Hamster Ovary (CHO) cell line.
Results: The cell growth, cell viability and cell
viabilities were comparable between ambrTM,10 and
200L Bioreactors200L Bioreactors.
Case Study 3: This protein molecule had two Isodimers (A and B). The levels of Isodimers A
and B were a product quality attribute.
Results: Ratio of Isodimers A
and B were similar (± 5% of
mean values) across ambrTM , 10
and 200L Bioreactors.
 The process decisions and results from ambrTM were reproducible to the
results in other scales bioreactors.
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.p p
PART C:
Control for process pH and DO during Cell Culture Process Development
 pH control in ambrTM is established using the
automated liquid handler based base additions
when pH drops below the pH set pointwhen 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 drift.
CO2: 0 - 1.24 mL/min. Delivered on demand to control pH.
O2 : 0 - 1.24 mL/min. Delivered on demand to control dissolved oxygen.
N : 0 1 24 mL/min Flow rate is constantN2 : 0 - 1.24 mL/min. Flow rate is constant.
 Online profiles for process pH (top Online profiles for process pH (top
figure) and DO (bottom 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 samplingcorresponded to bioreactor sampling,
Liquid additions and Sampling.
 All these disturb the headspace and
l h ki l Th i falter the working volume. The time for
the DO traces to equilibrate to setpoint
after such manipulations would depend
on the controller setup.p
Case Study 4: 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
b ™ t l t dambr™ system was evaluated.
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 > 2folds as
opposed to default manufacturer values , the pH drifts were reduced by 23 and 47 % of initial
value, respectively.value, respectively.
Results: The DO set points were changed to 80% from 20 and 40%, respectively and
changed back to original values The level for DO was maintained at 80% for duration of 6changed back to original values. The level for DO was maintained at 80% for duration of 6
hours and returned to original set points 20 and 40% in ≈ 90 and 120 mins, respectively.
 Th p bilit f ind in d i ti n n h lp in d i nin r t The capability of inducing deviations can help in designing worst-case
experiments. It enables to test operating limits with respect to particular
key operational parameters (DO, pH) in a process.
 The combination of pH and DO control and an automated liquid handling system in
ambrTM system overcomes major limitations of conventional small-scale cultures vessels
Conclusions
ambr system overcomes major limitations of conventional small scale cultures vessels
especially shake flasks.
 The single-use, pre-calibrated, and instrumented vessels used in ambrTM system provides
a platform for high-throughput in cell culture process development while mimicking a
stirred-tank bioreactor environment.
 The reproducibility of key observations observed in historical process developmentT e ep od c b ty o ey obse vat o s obse ved sto ca p ocess deve op e t
demonstrated that ambr™ is capable of providing predictive results under bioreactor
relevant process conditions.
R d ibili l bili d h bili f h d b i h Reproducibility, scalability and the ability of the system to respond to perturbations show
ambrTM to be adequate to consider this system for early and late stages of cell culture
process development.
 The studies at KBI aimed to demonstrate the utility of the ambr™ system as a
high- throughput bioreactors that can offer the realistic possibility of decreasing the
process development time for investigational biopharmaceuticals to reach the clinic.
Process
Characterization
Commercial ProcessProcessCell LineDiscovery Manufacturing
Biopharmaceutical Development Process.
Characterization
and Validation
DevelopmentDevelopmentDevelopment
y
Stage
RAPID PRODUCT DEVELOPMENT AT KBI
Manufacturing
ambrTM
Process Development
(Design Space & Optimization)
Cell Line DevelopmentDiscovery Stage Manufacturing
• Platform Downstream Processes
• High-throughput Resin Screening
• Single - Use Technology
TM The combination of methodologies such as ambrTM, Platform Downstream
Processes, High-throughput Resin Screening and use of Single-use technology
can significantly shorten the window for process development and
f t imanufacturing.
Acknowledgements
• Joe McMahon President and CEO
• Abhinav Shukla, Ph.D. VP, Process Development and Manufacturing
• Sigma Mostafa Ph D Director Process DevelopmentSigma Mostafa, Ph.D. Director, Process Development
• Haiou Yang, Ph.D. Scientist II, Process Development
• Christopher Miller Scientist II, Process Development
• Anushya Mani Scientist I Process Development• Anushya Mani Scientist I, Process Development
• Joe Jirka Product Specialist, TAP Biosystems
 Process Development Team at KBI Process Development Team at KBI
ThanksThanks
Questions??Questions??

More Related Content

PDF
High-throughput and Automated Process Development for Accelerated Biotherapeu...
PPTX
Application of Q R M in Manufacturing Operations
PDF
An Integrated Approach to Ensure Viral Vector and Gene Therapy Commercial Rea...
PPT
Common technical document (CTD – ICH)
PDF
Pharma regulatory affairs
PPTX
Standard operating procedure in pharmaceutical industries rashmi nasare
PDF
SAE Narrative Writing
PDF
Production and purification of Viral vectors for gene and cell therapy appli...
High-throughput and Automated Process Development for Accelerated Biotherapeu...
Application of Q R M in Manufacturing Operations
An Integrated Approach to Ensure Viral Vector and Gene Therapy Commercial Rea...
Common technical document (CTD – ICH)
Pharma regulatory affairs
Standard operating procedure in pharmaceutical industries rashmi nasare
SAE Narrative Writing
Production and purification of Viral vectors for gene and cell therapy appli...

What's hot (20)

PDF
Assessment on the effectiveness of the universally accessible cheaper and qua...
PPTX
Identification of pharmaceuticals by raman spectroscopy
PDF
ISO 22000:2018 FSMS manual template (preview)
PPTX
Quality by Design
PPTX
Turacoz - Risk Management Plan ( Regulatory Writing )
PPT
Schedule L1
PPTX
Presentation on ICH guidelines Q5A (R1) and Q4B Annex 2 (R1)
PPTX
Comparision of US & Indian GMP's
PDF
Excipients presentation-part 1-definition and regulation
PDF
Module 3 pharmaceutical development 2
PPTX
Progeny LIMS
PPS
CSV Audit Presentation
DOC
Pharmacovigilance officer performance appraisal
PPTX
Medwatch and FAERS database
PPT
ICH GUIDELINES FOR STABILITY Q1A powerpoint.ppt
PDF
Continuous Manufacturing - Issues and Answers
PPT
Nitrosamines: A Review.ppt
PDF
Viral safety of biologics: What's changing with the ICH Q5A revision?
PPTX
Elements of a Quality System for Medical Devices
PDF
Bio cmc development
Assessment on the effectiveness of the universally accessible cheaper and qua...
Identification of pharmaceuticals by raman spectroscopy
ISO 22000:2018 FSMS manual template (preview)
Quality by Design
Turacoz - Risk Management Plan ( Regulatory Writing )
Schedule L1
Presentation on ICH guidelines Q5A (R1) and Q4B Annex 2 (R1)
Comparision of US & Indian GMP's
Excipients presentation-part 1-definition and regulation
Module 3 pharmaceutical development 2
Progeny LIMS
CSV Audit Presentation
Pharmacovigilance officer performance appraisal
Medwatch and FAERS database
ICH GUIDELINES FOR STABILITY Q1A powerpoint.ppt
Continuous Manufacturing - Issues and Answers
Nitrosamines: A Review.ppt
Viral safety of biologics: What's changing with the ICH Q5A revision?
Elements of a Quality System for Medical Devices
Bio cmc development
Ad

Viewers also liked (20)

PDF
Scalability of a Single-Use Bioreactor Platform for Biopharmaceutical Manufac...
PDF
Biopharmaceutical Formulation Development CM3 Implementation and Initial Testing
PDF
Optimization of Glycosyation & Charge Distribution Through Culture Parameters...
PDF
Debottlenecking Manufacturing Capacity: Initiating cell culture manufacturing...
PDF
Platforms for mAb Commercialization
PDF
KBI Case Studies: Process Development
PDF
Scale-up & Tech Transfer from Non-disposable to Fully Disposable Systems
PDF
Integrated utilization of high-throughput bioreactors & high-throughput analy...
PDF
A Vaccine Approach against HIV-1, Manufacturing Env proteins: from Bench to B...
PDF
High Throughput PEGylation Process Development – Screening & Optimization Stu...
DOCX
Evolution of mAb Downstream Platforms
PDF
Managing Raw Material Variability Over the Life-cycle of a Molecule
PDF
Development of Analytical Control Strategies for L-DOS47, a Novel Antibody-En...
PDF
A Comparison of Protein A Chromatographic Stationary Phases
PDF
Evaluation of Established & New Viral Filters for a Monoclonal Antibody Platf...
PDF
A Comparison of Multimodal Chromatographic Resin: Protein Binding & Selectivity
PDF
Up to Speed: Cell Culture Development. European Biopharmaceutical Review July...
PDF
Importance of Understanding the Physical State of Excipients in a Freeze Drie...
PPTX
A Comparison of Multimodal Chromatography Resin: Case Study
PDF
Using Selective Washes to Solve a Purification Issue Involving a Host Cell Pr...
Scalability of a Single-Use Bioreactor Platform for Biopharmaceutical Manufac...
Biopharmaceutical Formulation Development CM3 Implementation and Initial Testing
Optimization of Glycosyation & Charge Distribution Through Culture Parameters...
Debottlenecking Manufacturing Capacity: Initiating cell culture manufacturing...
Platforms for mAb Commercialization
KBI Case Studies: Process Development
Scale-up & Tech Transfer from Non-disposable to Fully Disposable Systems
Integrated utilization of high-throughput bioreactors & high-throughput analy...
A Vaccine Approach against HIV-1, Manufacturing Env proteins: from Bench to B...
High Throughput PEGylation Process Development – Screening & Optimization Stu...
Evolution of mAb Downstream Platforms
Managing Raw Material Variability Over the Life-cycle of a Molecule
Development of Analytical Control Strategies for L-DOS47, a Novel Antibody-En...
A Comparison of Protein A Chromatographic Stationary Phases
Evaluation of Established & New Viral Filters for a Monoclonal Antibody Platf...
A Comparison of Multimodal Chromatographic Resin: Protein Binding & Selectivity
Up to Speed: Cell Culture Development. European Biopharmaceutical Review July...
Importance of Understanding the Physical State of Excipients in a Freeze Drie...
A Comparison of Multimodal Chromatography Resin: Case Study
Using Selective Washes to Solve a Purification Issue Involving a Host Cell Pr...
Ad

Similar to High Throughput Bioreactor Mimetic in Early and Late Stage Process Development (20)

PDF
High-throughput Miniaturized Bioreactors for Cell Culture Process Developmen...
PDF
Undergraduate Thesis - Joel John
PDF
Next Generation Recombinant Protein Manufacturing
PDF
Scalability of Cell Culture Processes in Single-use Bioreactors using Differe...
PDF
Continuous Biomanufacturing Innovative Technologies And Methods Subramanian
PDF
Cata_Upstream_S--1526-e
PDF
Getting Biopharmaceutical Production Processes Right the First Time
PPT
Seth Rodgers - High Throughput Cell Culture Platform for Bioprocess Optimizat...
PPTX
Bioreactor
PDF
Modification of basic bioreators.pdf sff
PDF
Webinar: Novel Perfusion Filter and Controller for N-1 Application
PDF
Webinar: Novel Perfusion Filter and Controller for N-1 Application
PPT
Biochemical engineering notes for biotechnology applications
PDF
Understanding and Controlling Bioprocess Variation | Parker domnick hunter
PPTX
Cell Culture Company - FY22 Overview
PDF
Development of novel chemically defined media for CHO cell applications
PDF
Cell culture
PDF
Celonic presentation on VIPS - BPI Boston (Sept 2019)
PPTX
Class Lecture 3_Bioprocess Engineering.pptx
PPTX
Industrial Bioprocessing webinar.pptx
High-throughput Miniaturized Bioreactors for Cell Culture Process Developmen...
Undergraduate Thesis - Joel John
Next Generation Recombinant Protein Manufacturing
Scalability of Cell Culture Processes in Single-use Bioreactors using Differe...
Continuous Biomanufacturing Innovative Technologies And Methods Subramanian
Cata_Upstream_S--1526-e
Getting Biopharmaceutical Production Processes Right the First Time
Seth Rodgers - High Throughput Cell Culture Platform for Bioprocess Optimizat...
Bioreactor
Modification of basic bioreators.pdf sff
Webinar: Novel Perfusion Filter and Controller for N-1 Application
Webinar: Novel Perfusion Filter and Controller for N-1 Application
Biochemical engineering notes for biotechnology applications
Understanding and Controlling Bioprocess Variation | Parker domnick hunter
Cell Culture Company - FY22 Overview
Development of novel chemically defined media for CHO cell applications
Cell culture
Celonic presentation on VIPS - BPI Boston (Sept 2019)
Class Lecture 3_Bioprocess Engineering.pptx
Industrial Bioprocessing webinar.pptx

More from KBI Biopharma (20)

PDF
Data Collection on the ProteinSimple Maurice: Driving Compliance with the Emp...
PDF
Integration of Cell Line and Process Development to Expedite Delivery of Bisp...
PDF
Debottlenecking Manufacturing Capacity Using High Seed Density Production Pro...
PDF
Application and Adaptation of Platform and Alternative Purification Steps to ...
PDF
Primary Recovery & Harvest Processes for non-mAb Recombinant Proteins
PDF
Compressed Timelines for Breakthrough Therapies: Impact on Process Characteri...
PDF
Speed to GMP: Moving from Rapid Process Development to High Throughput Tech T...
PPTX
Implementation of End-to-End Disposable Single Use Systems for Rapid Fermenta...
PDF
Host Cell Protein Analysis by Mass Spectrometry | KBI Biopharma
PDF
Handling High Titer Processes and Strategies for DSP Facility Fit | KBI Biop...
PDF
Octet Potency Assay: Development, Qualification and Validation Strategies
PDF
Fine-tuning your purification process: Using mechanistic modeling of chromato...
PDF
HIV Vaccines Process Development & Manufacturing - Pitfalls & Possibilities
PDF
Calorimetry study of a mAb that precipitates upon thermal denaturation
PDF
Size-Exclusion Chromatography with On-Line Light-Scattering, Absorbance, and ...
PDF
Effects of Additives on Reversibility of Thermal Unfolding
PDF
Analysis of Aggregation, Stability, and Lot Comparability by Sedimentation Ve...
PDF
New Software Methods Enhance Sedimentation Velocity Analysis of Protein Aggre...
PDF
Online Size-Exclusion High-Performance Liquid Chromatography Light Scattering...
PDF
Some Biophysical Methods for Demonstrating Comparability of Conformation and ...
Data Collection on the ProteinSimple Maurice: Driving Compliance with the Emp...
Integration of Cell Line and Process Development to Expedite Delivery of Bisp...
Debottlenecking Manufacturing Capacity Using High Seed Density Production Pro...
Application and Adaptation of Platform and Alternative Purification Steps to ...
Primary Recovery & Harvest Processes for non-mAb Recombinant Proteins
Compressed Timelines for Breakthrough Therapies: Impact on Process Characteri...
Speed to GMP: Moving from Rapid Process Development to High Throughput Tech T...
Implementation of End-to-End Disposable Single Use Systems for Rapid Fermenta...
Host Cell Protein Analysis by Mass Spectrometry | KBI Biopharma
Handling High Titer Processes and Strategies for DSP Facility Fit | KBI Biop...
Octet Potency Assay: Development, Qualification and Validation Strategies
Fine-tuning your purification process: Using mechanistic modeling of chromato...
HIV Vaccines Process Development & Manufacturing - Pitfalls & Possibilities
Calorimetry study of a mAb that precipitates upon thermal denaturation
Size-Exclusion Chromatography with On-Line Light-Scattering, Absorbance, and ...
Effects of Additives on Reversibility of Thermal Unfolding
Analysis of Aggregation, Stability, and Lot Comparability by Sedimentation Ve...
New Software Methods Enhance Sedimentation Velocity Analysis of Protein Aggre...
Online Size-Exclusion High-Performance Liquid Chromatography Light Scattering...
Some Biophysical Methods for Demonstrating Comparability of Conformation and ...

Recently uploaded (20)

PPTX
Neuropathic pain.ppt treatment managment
PPTX
CHEM421 - Biochemistry (Chapter 1 - Introduction)
PPTX
Clinical approach and Radiotherapy principles.pptx
PPTX
2 neonat neotnatology dr hussein neonatologist
PDF
Cardiology Pearls for Primary Care Providers
PPT
Infections Member of Royal College of Physicians.ppt
PPTX
Morphology of Bacterial Cell for bsc sud
PPTX
Electrolyte Disturbance in Paediatric - Nitthi.pptx
PPT
MENTAL HEALTH - NOTES.ppt for nursing students
PPTX
vertigo topics for undergraduate ,mbbs/md/fcps
PPTX
Acute Coronary Syndrome for Cardiology Conference
PPT
STD NOTES INTRODUCTION TO COMMUNITY HEALT STRATEGY.ppt
PPTX
the psycho-oncology for psychiatrists pptx
PPTX
ONCOLOGY Principles of Radiotherapy.pptx
DOCX
PEADIATRICS NOTES.docx lecture notes for medical students
PDF
Copy of OB - Exam #2 Study Guide. pdf
PPTX
IMAGING EQUIPMENiiiiìiiiiiTpptxeiuueueur
PPT
neurology Member of Royal College of Physicians (MRCP).ppt
PPTX
preoerative assessment in anesthesia and critical care medicine
PPT
Obstructive sleep apnea in orthodontics treatment
Neuropathic pain.ppt treatment managment
CHEM421 - Biochemistry (Chapter 1 - Introduction)
Clinical approach and Radiotherapy principles.pptx
2 neonat neotnatology dr hussein neonatologist
Cardiology Pearls for Primary Care Providers
Infections Member of Royal College of Physicians.ppt
Morphology of Bacterial Cell for bsc sud
Electrolyte Disturbance in Paediatric - Nitthi.pptx
MENTAL HEALTH - NOTES.ppt for nursing students
vertigo topics for undergraduate ,mbbs/md/fcps
Acute Coronary Syndrome for Cardiology Conference
STD NOTES INTRODUCTION TO COMMUNITY HEALT STRATEGY.ppt
the psycho-oncology for psychiatrists pptx
ONCOLOGY Principles of Radiotherapy.pptx
PEADIATRICS NOTES.docx lecture notes for medical students
Copy of OB - Exam #2 Study Guide. pdf
IMAGING EQUIPMENiiiiìiiiiiTpptxeiuueueur
neurology Member of Royal College of Physicians (MRCP).ppt
preoerative assessment in anesthesia and critical care medicine
Obstructive sleep apnea in orthodontics treatment

High Throughput Bioreactor Mimetic in Early and Late Stage Process Development

  • 1. High throughput bioreactor mimetic in l d l t t d l tearly and late stage process development American Chemical Society – Biochemical Technology (BIOT) Division 245th – ACS National Meeting, New Orleans, LA Shahid Rameez, Ph.D.Shahid Rameez, Ph.D. Scientist I, Process Development KBI Biopharma Inc, Durham, NCp
  • 2. Overview Ambr System Bioreactor Mimetic In process Mimetic KBI Evaluation p Activities & Design Space Evaluation Experimental Design in Early and Late C t l St t i y Stage Process Development Control Strategies
  • 3.  A key bottleneck in biopharmaceutical development has been they p p rapid development of robust and scalable manufacturing processes that can permit accelerated progress of products into clinical trials.  Innovations in this area can have a very significant impact on the overall economics of biopharmaceutical drug development by d i h i i k h h li idecreasing the time it takes to reach the clinic.  Mammalian cell culture processes typically have the longestp yp y g experimental duration with 2-3 weeks being a typical duration for the production bioreactor step with additional time spent on the seed culturescultures.
  • 4.  Shake flasks provide the capability to perform high throughput experiments, but with an inability to control process parameters likeexperiments, but with an inability to control process parameters like agitation rate, dissolved oxygen (DO) and pH.  Th t l h l h d l i b t ffi i t These parameters play a huge role when developing a robust, efficient cell culture process which dictates the product quality and yield.  Moreover, reproducibility and scalability of process and culture performance is a pre-requisite for successful and efficient process development at a scale down level.development at a scale down level.  At KBI we did case studies evaluating the ambr™ system (an a tomated micro scale bioreactor s stem) to establish the roleautomated micro-scale bioreactor system) to establish the role this system could play in accelerating biotech drug development.
  • 5. Automated Miniaturized Bioreactors 1mL tips ambrTM Technology 1mL or Liquid Handler 4mL tips Handler Used Tips Discard Culture stations; each holding 12 bioreactors
  • 6. ambrTM Deck Layout Culture stations 1ml tips 4ml tips4ml tips 24 deep-well plate Tip box lid Plate lid
  • 7. The Vessel Vessel Cap: In-line filter on gas supply DO sensor on gas supply Impeller pH sensorp
  • 8. Culture Station Nomenclature Culture station 1 (CS1) Culture station 2 (CS2) CS1-1 CS1-2 CS1-3 CS1-4 CS1-5 CS1-6 Culture station 1 (CS1) CS2-1 CS2-2 CS2-3 CS2-4 CS2-5 CS2-6 Culture station 2 (CS2) 7 8 9 10 11 12 7 8 9 10 11 12 CS1-7 CS1-8 CS1-9 CS1-1 CS1-1 CS1-1 CS2-7 CS2-8 CS2-9 CS2-1 CS2-1 CS2-1 Id l ki l i 13mL W ki l i 11 15mLIdeal working volume is 13mL; Working volume range is 11 – 15mL Things to consider: – Feed strategy and Sampling strategyFeed strategy and Sampling strategy – Low volumes – gas entrainment / vortexing – High volumes – Limits kLa.
  • 9. PART 1: Reproducibility for Results and Key Observations during Cell Culture Process Development  The processes evaluated in ambrTM were previously developed from a rigorous cell culture process development performed in classical bioreactors of various scales. The process were successfully carried in bioreactors across various scales: 2L, 10L d 200L10L and 200L.  This study aimed at studying the reproducibility of the key observations of the processes in ambrTM. Thus a reverse engineering approach was adopted, where we were cognizant about the outcomes from most of the experiments as far as inducing process variations was concerned.  The reproducibility of key historical results in ambrTM would corroborate towards its capability as a high throughput bioreactor mimetic in cell culture process development.
  • 10. K Ob i f Hi i l D Case Study 1: Reproducibility evaluation for the production of a monoclonal antibody in a recombinant Chinese Hamster Ovary (CHO) cell line. Key Observations from Historical Data: • Temperature Shift during the cell culture process was found to be the most important process factor to regulate the productivity of the antibody titer. • 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 for feed. • A highly basic and a critical feed, referred here as FDX, had to be added without pre- neutralization with acids to avoid osmolality increase in cultures. Thus, a better control had to be established in the bioreactors to control the pH drift with addition of FDX. h h d b b h d hThis was achieved in classical bioreactors by tuning the PID controllers and with regulation in cascade feedback gassing of CO2 and Air.
  • 11. Results: Both lower pH set-points and Temperature Shift showed higher cell growth, better cell viabilities. DO as suspected at negligible effect on cell growth and viability. Time courses for viable cell growth and viability 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 ambr 24. The error bars show the standard deviationdeviation.
  • 12. Results: Both lower pH set-points and 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 bi h i l d lbiopharmaceutical development.
  • 13. PART B: Scalability Assessment in Cell Culture Process Development Case Study 2: Comparison across scales for the production of a monoclonal antibody in a recombinant CHO cell line. Ambr (n = 3). 2L (n = 1). 10 ( 4)10L (n = 4). 200L (n = 1). • Harvest Titers within 1 5 1 7 g/L• Harvest Titers within 1.5 -1.7 g/L across all scales. Comparison of time courses for viable cell growth and viability for recombinant CHO cell line in ambrTM and other scales bioreactors: 2, 10L Glass bioreactors and 200L disposable bioreactor.p
  • 14. Case Study 3: Comparison across scales for the production of a protein molecule in a recombinant Chinese Hamster Ovary (CHO) cell line. Results: The cell growth, cell viability and cell viabilities were comparable between ambrTM,10 and 200L Bioreactors200L Bioreactors.
  • 15. Case Study 3: This protein molecule had two Isodimers (A and B). The levels of Isodimers A and B were a product quality attribute. Results: Ratio of Isodimers A and B were similar (± 5% of mean values) across ambrTM , 10 and 200L Bioreactors.  The process decisions and results from ambrTM were reproducible to the results in other scales bioreactors. 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.p p
  • 16. PART C: Control for process pH and DO during Cell Culture Process Development  pH control in ambrTM is established using the automated liquid handler based base additions when pH drops below the pH set pointwhen 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 drift. CO2: 0 - 1.24 mL/min. Delivered on demand to control pH. O2 : 0 - 1.24 mL/min. Delivered on demand to control dissolved oxygen. N : 0 1 24 mL/min Flow rate is constantN2 : 0 - 1.24 mL/min. Flow rate is constant.
  • 17.  Online profiles for process pH (top Online profiles for process pH (top figure) and DO (bottom 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 samplingcorresponded to bioreactor sampling, Liquid additions and Sampling.  All these disturb the headspace and l h ki l Th i falter the working volume. The time for the DO traces to equilibrate to setpoint after such manipulations would depend on the controller setup.p
  • 18. Case Study 4: 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 b ™ t l t dambr™ system was evaluated. 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 > 2folds as opposed to default manufacturer values , the pH drifts were reduced by 23 and 47 % of initial value, respectively.value, respectively.
  • 19. Results: The DO set points were changed to 80% from 20 and 40%, respectively and changed back to original values The level for DO was maintained at 80% for duration of 6changed back to original values. The level for DO was maintained at 80% for duration of 6 hours and returned to original set points 20 and 40% in ≈ 90 and 120 mins, respectively.  Th p bilit f ind in d i ti n n h lp in d i nin r t The capability of inducing deviations can help in designing worst-case experiments. It enables to test operating limits with respect to particular key operational parameters (DO, pH) in a process.
  • 20.  The combination of pH and DO control and an automated liquid handling system in ambrTM system overcomes major limitations of conventional small-scale cultures vessels Conclusions ambr system overcomes major limitations of conventional small scale cultures vessels especially shake flasks.  The single-use, pre-calibrated, and instrumented vessels used in ambrTM system provides a platform for high-throughput in cell culture process development while mimicking a stirred-tank bioreactor environment.  The reproducibility of key observations observed in historical process developmentT e ep od c b ty o ey obse vat o s obse ved sto ca p ocess deve op e t demonstrated that ambr™ is capable of providing predictive results under bioreactor relevant process conditions. R d ibili l bili d h bili f h d b i h Reproducibility, scalability and the ability of the system to respond to perturbations show ambrTM to be adequate to consider this system for early and late stages of cell culture process development.  The studies at KBI aimed to demonstrate the utility of the ambr™ system as a high- throughput bioreactors that can offer the realistic possibility of decreasing the process development time for investigational biopharmaceuticals to reach the clinic.
  • 21. Process Characterization Commercial ProcessProcessCell LineDiscovery Manufacturing Biopharmaceutical Development Process. Characterization and Validation DevelopmentDevelopmentDevelopment y Stage RAPID PRODUCT DEVELOPMENT AT KBI Manufacturing ambrTM Process Development (Design Space & Optimization) Cell Line DevelopmentDiscovery Stage Manufacturing • Platform Downstream Processes • High-throughput Resin Screening • Single - Use Technology TM The combination of methodologies such as ambrTM, Platform Downstream Processes, High-throughput Resin Screening and use of Single-use technology can significantly shorten the window for process development and f t imanufacturing.
  • 22. Acknowledgements • Joe McMahon President and CEO • Abhinav Shukla, Ph.D. VP, Process Development and Manufacturing • Sigma Mostafa Ph D Director Process DevelopmentSigma Mostafa, Ph.D. Director, Process Development • Haiou Yang, Ph.D. Scientist II, Process Development • Christopher Miller Scientist II, Process Development • Anushya Mani Scientist I Process Development• Anushya Mani Scientist I, Process Development • Joe Jirka Product Specialist, TAP Biosystems  Process Development Team at KBI Process Development Team at KBI