cell culture technology for pharmaceutical and...
TRANSCRIPT
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Sadettin S Ozturk
Cell Culture Technology forPharmaceutical and Cellular
Therapies
Sadettin S. Ozturk, Ph.D.Sadettin S. Ozturk, Ph.D.Centocor Centocor Inc.Inc.
200 Great Valley Parkway, Malvern, PA 19355200 Great Valley Parkway, Malvern, PA 19355
Sadettin S Ozturk
Outline
1. Introduction to Monoclonal Antibodies
2. Production of Monoclonal Antibodies
3. Introduction of Centocor
4. Autoimmune disorders
5. Development of Monoclonal Antibody based Pharmaceutical Therapies
6. Case study: Fed-batch Process development for Monoclonal Antibodies
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Immune Response as First Line of Defense
When a pathogen (bacteria, foreign proteins, virus,.) enters the blood stream it is recognized, attacked, and eliminated by a sophisticated defense mechanism: Body’s Immune Response
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Immune System: The Body's First Line of Defense
Lymphatic vessels form a circulatory system that operates in close partnership with blood circulation.
Organs and tissues of the immune system dot the body in a protective network of barriers to infection.
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The antibody – a.k.a “Immunoglobulin”
-The Variable region is different for each antibody and determines its specificity.
-The Constant region is identical for each type of antibody and allows recognition by your immune cells.
Antibodies are produced by B-cells as part of immune response. Each antibody is specific to a specific antigen
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Evolution of Antibody Technology:Development of Antibody Based Medicines
• Utilization of antibodies as medicines took some time:– B-cells cannot be expanded in vitro for practical purposes – It is difficult to find out which B-cell makes a specific antibody
• Kohler and Milstein discovered Hybridoma Technology and cloning in 1975: A revolution in antibody technology– Hybridoma cells (a fusion of B-cell and myeloma cell) can be expanded
indefinitely– Utilization of cloning techniques allows to isolate cells that make a
specific antibody: These antibodies are called Monoclonal Antibodies (Mab)
• Expansion of hybridoma cells in vivo (mouse) or in vitro (bioreactors) allowed the development of first MAbs
• Over the last 30 years antibody technology was further developed– Engineering of antibodies to make them more “human”– To use cell lines other than hybridoma cells (CHO, NS0, etc)– The use of antibody fragments and fusion proteins– The use of antibodies for targeted drug delivery
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Murine IgG
ChimericIgG
Fab
Fc
Humanized IgG Fully Human IgG
Current
Products in
Development
Engineering of Antibodies
“Humanization” of antibody minimizes/eliminates immune reaction when injected to the patients
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Monoclonal Antibodies as Medicines
• There are 18 approved antibody treatments in the market for:• Autoimmune disorders• Cancer• Asthma• Organ rejection
• Sales of antibodies is expected to be $13 Billion in 2005• There are 500 new antibody products in development• There are 75 new antibodies in clinical trials• Sales of antibodies is expected to be $26 Billion in 2010• Some of the indications require as high as 2,000 kg/year product• These antibodies are produced in large (20,000L) bioreactors
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Therapeutic Antibodies Approved to Date
* Nature Biotechnology, Sept. 2005, 23(9), p.1075
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Production of Monoclonal Antibodies
Seed Bioreactor
50L
Production Bioreactors
300L, 1500L, 5000L, 20,000L
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InoculumBioreactor
ProductionBioreactor
Monoclonal Antibody Production ProcessBioreactor and Product Capture
Monoclonal Antibody Production ProcessBioreactor and Product Capture
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Monoclonal Antibody Production Process
Monoclonal Antibody Production Process
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Shipment toFill and
Finish Site
Monoclonal Antibody ProductionProcess
Monoclonal Antibody ProductionProcess
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Production Bioreactors: Continuous Perfusion Operation
• Cells are retained in the bioreactor by physical means
• Cells grow, stay in the bioreactor, and produce proteins
• Media is added and harvest is collected continuously
• Can be operated for months• Usually compact bioreactors
(1000L)
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Production Bioreactors: Batch Operation
• Inoculate with media and cells
• Cells grow and produce proteins
• All of the contents are harvested after typically 2 weeks
• Usually very large bioreactors (20,000L)
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Purification of Monoclonal Antibodies using Column Chromatography
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Concentration and Diafiltration of Monoclonal Antibodies
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Centocor : An Antibody Company
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Centocor Timelines
1999
1998Centocor Founded
IPO Raised $21 Million; First Diag.
Product Approved by
FDA
Leiden Mfg. Plant Opens
Marketing Alliance with
Lilly for ReoPro®
Launched ReoPro®
RETAVASE®
Approved; REMICADE®
Launched in Crohn’s
In the past five years, sales have grown from $500 million to over $3 billion.
1979 1987 1995
1982 1993
Merger with
REMICADE®
Launched in Rheumatoid
Arthritis
1999
2004
REMICADE®
Launched in ERA & AS 2005
REMICADE®
launches in psoriasis
(OUS), ulcerative
colitis (U.S.) and PsA
(U.S.)
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Centocor Products
• Launched 1998– Approved in over 80 countries
World Wide– 2004 WW sales $2.63 Billion– Indications: RA / CD / AS /
PsA/UC
• Launched 1995– Approved in over 50
countries World Wide– 2004 WW sales $363Million – Indications: PCI
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REMICADE® Approvals
1999 2000 2001 2002 2003 2004 2005 2006
Rheumatoid Arthritis –physical function in failed methotrexate
patientsRheumatoid Arthritis –structural damage
Psoriatic ArthritisCrohn’s
Disease –luminal CD
Rheumatoid Arthritis – signs &
symptoms of RA, inhibiting x-ray
diseases progression, and improving physical functioning in patients not previously treated
with methotrexate
Rheumatoid Arthritis –signs and symptoms
Crohn’s Disease
Ulcerative Colitis
1998
U.S
.E
U
Crohn’s Disease –fistulizing
Ankylosing Spondylitis
Crohn’s Disease –fistulizing
Rheumatoid Arthritis –physical function in failed methotrexate
patients
Rheumatoid Arthritis –structural damage
Crohn’s Disease –
luminal CD
Ankylosing Spondylitis
Crohn’s Disease –fistulizing
Psoriatic Arthritis
Psoriasis (OUS)
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Number of Patients TreatedWorldwide With REMICADE®
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Autoimmune disorders:What Are They?
Disorders caused by an immune response against the body's own tissues.
Immune system disorders occur when the immune response is inappropriate, excessive, or lacking.
Rheumatoid arthritisCrohn’s DiseasePsoriasisMultiple sclerosis (MS)Systemic lupus erythematosus
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Autoimmune disorders: Rheumatoid Arthritis
inflammation begins in the tissue lining your joints and then spreads to the whole joint (hand joints are the most common site, but it can affect most joints in the body)
• muscle pain• deformed joints• Weakness• Fatigue• loss of appetite• weight loss• becoming confined to bed in severe cases
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Autoimmune disorders:Crohn's Disease
• Chronic autoimmune disease where immune cells attack any part of the gastrointestinal tract
• The lining of the intestine may ulcerate and form channels of infection, called fistulas
• Ulcerative colitis is a similar inflammation of the colon, or large intestine
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• Immune-mediated, genetic disease manifesting in the skin and/or the joints
• Psoriasis and psoriatic arthritis affect more than 4.5 million people in the United States
• A person's quality of life—including emotional health—can be seriously jeopardized
Autoimmune disorders: Psoriasis
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Autoimmune disorders:Multiple sclerosis (MS)
– weakness and trouble with coordination, balance, speaking, and walking
– paralysis– Tremors– numbness and tingling feeling in arms, legs, hands, and feet
Lupus– swelling and damage to the joints, skin, kidneys, heart,
lungs, blood vessels, and brain– “butterfly” rash across the nose and cheeks– rashes on other parts of the body– painful and swollen joints– sensitivity to the sun
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Autoimmune disorders:A lot of things can go wrong in the immune
system to result in autoimmune disorders• T cell proliferation and interferon production • Differentiation of T-cells• Cytokine production• Cytokine, receptor binding• B-cell differentiation• Antibody production• Migration of cells to the tissue
Antibodies can be used to intercept or block these events
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The use of antibody based treatment for Psoriasis
J Invest Dermatol. 2004 Dec;123(6):1037-44.
Psoriasis activity before and after treatment with a specific antibody: 0.1 mg/kg dose (1 week post-treatment [baseline not available] and 16 weekspost-treatment); 1.0 mg/kg dose (baseline and 16 weeks post-treatment)
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Development of Antibodies for Pharmaceutical Therapies
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Process Development Tech. Transfer
Review Approval
Reg. FilingPhase III Clinical Trials
Submit BLA
Preclinical Studies
Early Development
Phase I / II Clinical Trials
Drug Development
Late Development
Clinical Development
Assay Validation
Cell Line Selectionand Purif./Form. Dev. Clinical Manufacturing Process
ValidationLaunch
Preparation
Year-3
Year1
Year2
Year3
Year4
Year5
TargetResearch
Manufacturing InvestmentDecision
Antibody Development and Commercialization Process
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Pharmaceutical Development
Clinical
Identify Molecular
Target
Create New
Discovery Research
Molecular Entity
Initiate Clinical Trials
Cell Line Development
Media Development
Bioreactor Process Development
Cell Line Development
Media Development
Bioreactor Process Development
Develop Purification
Process
Make Clinical Supplies Develop Formulation
Steps in Drug Development
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Clone productgene cDNA
Insert intoexpressionplasmids
Cell Line Development-Gene-Promoter-Enhancer-Selectivemarker
Transfection
Clone selectionfor highproducing cells
Amplify,Clone,Select,
Amplify,Clone,Select,
Host Cell
DevelopmentCell bank (DCB)
Evaluate inBioreactors
MasterCell bank (MCB)
Master workingCell bank (MWCB)
Develop expression vector
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Media Development
• Cell culture medium contains:
Salts, trace elements, glucose, amino acids,other nutrients, vitamins, buffers, etc.
• Early media formulations used serum or other animal derived proteins (albumin)
• Issues related to safety (BSE), availability, and cost became driving force to eliminate serum and to develop animal product free (APF) (safer and economical)
• Today chemically defined medium (CDM) is a reality for many cell culture based processes (consistent and traceable)
• Most of the companies use specially formulated in-house proprietary media formulations for their processes (independence)
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Bioreactor Process Development
• Batch, fed-batch, and perfusion process options are in use for commercial production
• It is possible to get 5 g/L titers in fed-batch and about 50 MM cells/mL in perfusion
• Bioreactor process development involves– Optimization of culture environment
(pH, temperature, DO, CO2)– Optimization of media exchange rates– Development of feeding solutions and
feeding strategies
• Advances in biochemical engineering made it possible to grow animal cells in conventional bioreactors (no need for specialized systems)• Today stirred-tank based bioreactors are in operation at sizes up to 20,000L
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Process/Media
SelectionSystem Host cell
gpt/MHX
GS/MSXDHFR/MTX
Sp2/0
CHO-dhfr-NS0
CHOK1SV
Perfusion
Fed-batch
Neo/G418
Monoclonal Antibody
BatchCommercial
Proprietary
Therapeutic
Process Development Options
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� Cell line: CHOK1SV
� Glutamine Synthetase selection system
� Animal product free medium
� Fed-batch process in stirred tank bioreactors
� Optimized pH, temperature
� Optimized feeding schedule
� Process Scale-up
� Consistency
Case Study: Development of a Fed-batch Process for Monoclonal
Antibody Production
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Glutamine Synthetase (GS) catalyzes the biosynthesis of glutamine from glutamate and ammonia, providing the only pathway for L-glutamine formation in the cell
Glutamate + NH3 L-glutamine
ATP ADP + Pi
MSX
GS
MSX = L-Methionine Sulfoximine
In the absence of glutamine, the GS enzyme is essential for cell survival
Cell Line Development: Introduction/Selection System
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VH
GS
hCMV
VL
hCMV
CH3
CH1
CH2
Ck
Clone
by PCRAmplification
mRNA cDNA
- Start with a research cell line (expressing < 20 mg/L)
- Isolate RNA, reverse transcribe to generate cDNA
- Use sequence information from genomic constructs to
design PCR primers to isolate specific HC and LC cDNAs
- Clone cDNAs into Lonza GS vectors, pEE 6.4 and pEE 12.4
- Construct a GS ‘double-gene’ plasmidHC LC
11479 bp
CNTO X LC
SV40 poly A
SV40 poly A
Pvu I
Not I
Sal I
GS CNTO XDouble Gene
hCMV-IE promoter and intron
Kozak sequence
hCMV-IE promoter and intron
Kozak sequence
CNTO X HC
β-lactamase (Amp resistance)
GS cDNA
SV40 promoter
Cell Line Development: Schematic Overview of Plasmid Construction
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STATIC CULTURE Transfections3-6 weeks
200-300 transfectants
60-100 transfectants
1 week
2 weeks
96w plates
24w plates
Rank order clones by96w single-point ELISA
Rank order clones by24w Neph. (overgrow)
3-10 parental cell lines
SUSPENSION(shake flask culture)
SUBCLONES
3 weeks
3 weeks
8 weeks
3 weeks
6 weeks
Adapt to CD-CHO
Perform shake flask
growth profiles
Prepare and test DCBs
Bioreactorprocess development
1-3 parental cell lines
1-3 parental cell lines
3-10 parental cell lines
Subclone
Rank 24w (Neph.)
Adapt to CD-CHO8 weeks
3 weeks Perform shake flaskgrowth profiles
30-100 subclone cell lines
3-10 subclone cell lines
3-10 subclone cell lines
12-16 weeks
Cell Line Development: Process of Developing High Producing GS-CHO Cell Lines
~ 4.5 months ~ 6 months
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Cell Line Development: Clone Selection
Immuno-precipation method for rapid selection of high expression/ secretion clones:
Patent: WO 2005 / 020924 A2 (Publication date 10 March 2005)
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Automated Halo-Colony Picking
ClonePix interiorClonePix interior
HEPA filtration
Holder for 5 Culture dishes
Wash and
sterilise
Stacker for microplates
1µm encodersCCD camera
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Clone # 96w ELISA Titer 24w Neph Titer3 21 26.6 mg/L 76.0 mg/L4 23 20.3 mg/L 52.9 mg/L6 36 18.7 mg/L 61.8 mg/L
16 113 37.1 mg/L 67.5 mg/L20 123 25.3 mg/L 93.6 mg/L21 127 4.1 mg/L 59.1 mg/L22 134 25.3 mg/L 79.7 mg/L
Rank Order Clones: 96w ELISA / 24w Nephelometry
Cell Line Development: Transfection and Colony Screening
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- Expand in 24w, T-flasks, and cryopreserve- Adapt highest expressing cell lines to APF medium (CD-CHO)- Adapt to suspension culture in shake flasks- Perform 10-passage stability study- Perform growth profiles in shake flasks in APF medium- Transfer cell line(s) to bioreactor process development group
Specific Productivity
y = 18.055xR2 = 0.9474
y = 17.049xR2 = 0.9445
0
100
200
300
400
0 5 10 15 20 25
Integral of Viable Cells (E6/mL * days)
An
tib
od
y T
iter
(m
g/L
)
VCD vs. Days
0
1
23
4
5
0 1 2 3 4 5 6 7 8 9 10 11 12 13
Days
VC
D (
x 10
^6 c
ells
/mL
)
Titer Accumulation vs. Days
0
100
200
300
400
0 1 2 3 4 5 6 7 8 9 10 11 12 13
Days
Ant
ibod
y Ti
ter
(mg/
L)
Cell Line Development: RESULTS
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VCC C1180A Batch
Temp and pH DOE
0.000
0.500
1.000
1.500
2.000
2.500
3.000
3.500
4.000
4.500
0 2 4 6 8 10 12 14 16 18 20
Day
VC
C
H005H006H007H008H009H010J003J004J005J006
H00635 C7.2
H01036.5 C7.0
H00738 C6.8
H00938 C7.2
H00535 C6.8
J00338 C7.2
H00835 C7.2
J00435 C6.8
J00538 C6.8
J00636.5 C7.0
Fed-batch Process Development: Temperature and pH Optimization in Batch
Cultures
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% Viability C1180A Batch
Temp and pH DOE
0
20
40
60
80
100
120
0 5 10 15 20 25
Day
% V
iab
le
H005H006H007H008H009H010J003J004J005J006
H00635 C7.2
H00738 C6.8
H00938 C7.2
H01036.5 C7.0
H00535 C6.8
J00338 C7.2
J00435 C6.8
J00538 C6.8
J00636.5 C7.0
H00835 C7.2
Fed-batch Process Development: Temperature and pH Optimization in Batch Cultures
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C1180A Temp and pH DOE Titer Comparison
0.00
100.00
200.00
300.00
400.00
500.00
600.00
0 2 4 6 8 10 12 14 16 18 20
Day
Titer H005Titer H006Titer H007Titer H008Titer H009Titer H010Titer J003Titer J004Titer J005Titer J006
H00938 C7.2
H00635 C7.2 H008
35 C7.2
H01036.5 C7.0
H00738 C6.8
H00535 C6.8
J00338 C7.2
J00538 C6.8
J00636.5C7.0
J00435 C6.8
Fed-batch Process Development: Temperature and pH Optimization in Batch Cultures
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• GS-CHO Cell line producing a fully human antibody
• Animal Product Free Medium• pH, DO, and temperature set-points from batch
optimization study• Feeding solutions include
– Glucose, plant hydrolysate, MEM, NEAM, Vitamins, Specially formulated cocktails
• Feeding strategies include daily additions of pre-determined amounts to the bioreactor
Fed-Batch Process Development: Feeding Strategies
Fed-Batch Process Development: Feeding Strategies
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Fed-Batch Process Development: Feeding Strategies
CD CHO Fed Batch Viable Cell Density Comparison
0.00
1.00
2.00
3.00
4.00
5.00
6.00
7.00
8.00
9.00
0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19
Day
Via
ble
Cel
l Den
sity
(x1
0E6
cells
/mL
)
M04E001 M04E002 M04E003 M04E004 MO4E007 M04E008 M04D014 M04D015M04F038 M04F039 M04E031 M04F032
Glu, BRX, Nucleosides, PHyd
Glu, PHyd BioGro
BRX=MEM+NEM+Vitamins PHyd=Plant Hydrosylate
Glu, PHyd MEM, NEAM, GS
BatchGlu, PHyd
Glu, PHyd MEM
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Fed-Batch Process Development: Feeding Strategies
CD CHO Fed Batch Antibody Comparison
0
200
400
600
800
1000
1200
1400
1600
0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23
Day
An
tib
od
y (m
g/L
)
E001 E002 E003 E004 E007 E008 D014 D015
M04F038 M04F039 M04E031 M04F032
Glu, BRX, Nucleosides, PHyd
Glu, Phyd, BioGro
Glu, Phyd, MEM, NEAM, GS
Batch
Glu, PHyd
Glu, Phyd, MEM
BRX=MEM+NEM+VitaminsPHyd=Plant Hydrosylate
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Fed-Batch Process Development: Results
0
1
2
3
4
5
6
7
8
Maxim
um
Via
ble
cell
s, M
M/
mL
Bat
ch
Glu
, so
y
Glu
,soy
,MEM
Glu
, so
y,Bio
Gro
Glu
, so
y, M
EM
,N
EM
, G
S S
upp
Glu
, BRX,
soy,
nucl
eosi
des
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Fed-Batch Process Development: Results
0
200
400
600
800
1000
1200
1400
1600
IgG
, m
g/
L
Bat
ch
Glu
, so
y
Glu
,soy,
MEM
Glu
, so
y,Bio
Gro
Glu
, so
y, M
EM
,N
EM
, G
S S
upp
Glu
, BRX,
soy,
nucl
eosi
des
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Non-reduced Reduced
In-process Testing : Agilent 2100 Bioanalyzer
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Process Scale-up and Commercialization
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Process Scale-up and Consistency
0
1
2
3
4
5
6
7
8
9
10
0 2 4 6 8 10 12 14
Days
VC
C (
x10E
6 ce
lls/m
L)
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Process Scale-up and Consistency
0
500
1000
1500
2000
2500
0 2 4 6 8 10 12 14
Days
Tit
er (
mg
/L)
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Process Consistency: SDS-PAGE
ReducedReduced
Non-ReducedNon-Reduced
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Process Consistency: IEF
8.258.107.897.74
8.258.107.897.74
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Process Consistency: Tryptic Peptide Maps
Ref StdRef Std
Batch-1Batch-1
Batch-2Batch-2
Batch-3Batch-3
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Conclusions1. Monoclonal Antibodies evolved over the years to
become an essential part of biotechnology
2. Monoclonal Antibodies can be used as an effective therapy for immune disorders
3. There are several processing options for the manufacture of Monoclonal Antibodies. The final choice may depend on a variety of reasons
4. Development and manufacturing of Monoclonal Antibodies require extensive optimization, consistency, and comparability studies
5. It can be tedious, frustrating, costly, and very risky, but making a drug that can help people’s life is worth it.