Optimization of Glycosyation & Charge Distribution Through Culture Parameters & Supplements
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Transcript of Optimization of Glycosyation & Charge Distribution Through Culture Parameters & Supplements
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OPTIMIZATION OF GLYCOSYLATION AND
CHARGE DISTRIBUTION THROUGH CULTURE
PARAMETERS AND SUPPLEMENTS
Sigma Mostafa, Venkata Tayi, Brian Baker, James Smedley, Nate Oien,
Derek Ryan, Abhinav Shukla
Cell Culture Engineering XV
May 11, 2016
• Introduction – KBI workflow
• Case study 1 – PAT approach to meet charge
species target
• Case study 2 – Product quality toolbox
• Case study 3 – Impact of Cu2+ on product quality
• Conclusions
Outline
2 |
KBI Locations
3 |
KBI RTP
• Cell Culture Process Development
• Purification Process Development
• Microbial Process Development
• Analytical Development
KBI Boulder
• Microbial Process Development
• Microbial cGMP Manufacturing
• Analytical Development
KBI Durham
• Analytical and Formulation Dev.
• Cell Line Development
• Cell Culture cGMP Manufacturing
CLD 2%
Dev / Mfg 27%
CLD / Dev / Mfg 32%
Process Characterization
14%
Tech. Transfer/MFG
12%
Dev 11%
PD Supply 2%
Project Types
12%
58% 2%
14%
2% 2%
7% 2%
Molecule Types
Bispecific Ab mAb*
Growth factor Vaccine glycoprotein
Enzyme Recombinant Enzyme
PEGylated protein Fc-Fusion Protein
4 |
Distribution of 2015 Completed Projects: 50+ in
Development
*Includes 5 Biosimilars
Background
• Technology Transfer project
• CHOK1 cell line
• Medium & feeds are off-the shelf
• Limited historical data (n = 2 with varied
data)
• Acidic species desired level within 35 – 45%
5 |
Case Study 1: PAT approach to meet PQ target
• Cell growth and viability were comparable
across bench scale cultures
Case Study 1: PAT approach to meet PQ target
6 |
• Acidic species range was met only in portion of the
bench scale runs
• Other cell culture and PQ ranges were met by all the
runs
Case Study 1: PAT approach to meet PQ target
7 |
• Impact of culture length on acidic species was
investigated
• Acidic species was observed to decrease with
culture time
8 |
Case Study 1: PAT approach to meet PQ target
• At the 200L Demo Run stage daily WCX testing
was carried out to determine harvest day
9 |
Case Study 1: PAT approach to meet PQ target
• This PAT approach was implemented in the cGMP runs
• The three cGMP runs were harvested on three different
days based on acidic species level
Case Study 1: PAT approach to meet PQ target
10 |
• Acidic species levels were very similar for all 3
cGMP BDS
• Other product quality attributes were also within
acceptable range
Case Study 1: PAT approach to meet PQ target
11 |
• A PAT approach using a WCX assay led to a
successful cGMP campaign
• Variable harvest day, within a narrow range,
maintained other cell culture and product
quality attributes in range
• Cross functional collaboration was critical
for successful implementation of this
approach
Case Study 1: Results Summary
12 |
• KBI has an array of tools to customize
product quality
13 |
Case Study 2: Product Quality Toolbox
Galactose
Fucose
Mannose
Sialic Acid
Ratio of
main/
acidic/
basic
species
HMW & LMW
• Impact of key supplements on glycosylation
Case Study 2: Product Quality Toolbox
14
0
20
40
60
80
100
G0 FG0 G1 FG1 G2 FG2
2.0
80.4
11.9
0.6
%
No supplements
0
20
40
60
80
100
G0 FG0 G1 FG1 G2 FG2
7.1
44.9
2.6
35.2
5.5
%
Mn2+ + Uridine + Galactose
0
20
40
60
80
100
G0 FG0 G1 FG1 G2 FG2
29.2
55.3
2.3 8.2
0.5
%
Fucosylation inhibitor (2F-PAF)
0
20
40
60
80
100
G0 FG0 G1 FG1 G2 FG2
36.3
20.6 16.3 17.1
2.1 3.1
%
2F-PAF + Mn2+ + Uridine + Galactose
9/21/2016 15
0%
20%
40%
60%
80%
100%
37C 37C --> 32C
25.2 11.4
67.2
54.6
7.6
24.6
% Acidic % Main % Basic
Effect of temperature shift on charge variants distribution
• Temperature shift decreased the
acidic variants possibly due to
reduction of deamidation
• Temperature shift increased basic
variants possibly due to c-terminal
lysine residues
• Temperature shift to an optimized
value could produce the molecule
with desired profile
Case Study 2: Product Quality Toolbox
16 |
Case Study 2: Product Quality Toolbox
• Temperature shift decreased galactosylation
across clones
• A product quality toolbox was established as
a technology development project
• This toolbox has been successfully used in
multiple biosimilar and novel molecule
process development
17 |
Case Study 2: Results Summary
Background
• CHO DG44 derived vendor cell line
• Doubling time <20 hours
• Commercial off the shelf medium & feed
• KBI received a Phase I process that had
historically shown high variability
• Scope of project at KBI – Resupply and
further development
18 |
Case Study 3: Impact of Cu+2 on Product Quality
• Replicate cultures in 3L bioreactors showed lack
of reproducibility
• Reactor 2 had a ‘favorable’ pH correction on day 7
(upward); Reactor 1 had ‘unfavorable’ pH
corrections on days 7 and 10 (toward lower end of
pH dead-band).
Case Study 3
19 |
• Feed addition led to immediate lactate production
and associated pH drop (feed pH is neutral)
• Amount of pH drop after a feed varied from run to
run and could be as high as 0.25 pH unit
20 |
Case Study 3
6.60
6.70
6.80
6.90
7.00
7.10
7.20
7.30
7.40
Day 8 Feed Day 10 Feed
Day 12 Feed Day 14
Feed
• Re-supply Strategy
- Expand pH dead-band
- Glucose range
- Initial glutamine
- Feed addition rate
21 |
Case Study 3
• Shake flask was found to be a good model
to study the high lactate & rapid viability
decline
• Addition of Cu2+ was tested in shake flask
and found to be highly successful in
extending viability and increasing
productivity
22 |
Case Study 3: Impact of Cu+2 on Product Quality
Case Study 3: Impact of Feeds and Supplements in SF
23
0
5
10
15
20
25
30
35
40
45
0 2 4 6 8 10 12 14
VC
D (
10
6 c
ells/m
L)
Time (Days)
0
20
40
60
80
100
0 2 4 6 8 10 12 14V
iab
ilit
y (%
)
Time (Days)
Control with current Feed Current Feed + Cu supplementation
New Feed New Feed + Cu supplementation
New Feed + Amino Acid Cocktail + Cu supplementation
Case Study 3: Impact of Feeds and Supplements in SF
24
0
0.5
1
1.5
2
2.5
3
A B C D ETit
er
(g/L)
0
0.5
1
1.5
2
2.5
3
0 2 4 6 8 10 12 14
La
cta
te (
g/L)
Time (Days)
Control with current Feed Current Feed + Cu supplementation
New Feed New Feed + Cu supplementation
New Feed + Amino Acid Cocktail + Cu supplementation
Case Study 3: Impact of Feeds and Supplements in BRX
25
Control with current Feed New Feed + Amino Acid Cocktail + Cu supplementation
• Supplementation of culture with 400 nM
Cu2+ improved viability, titer, and process
reproducibility dramatically
Case Study 3: Results Summary
26 |
• High throughput, high sensitivity analytics
are essential for successful and efficient
process development
• Surrogate outputs, in place of complex
analytics such as mass spec, would enable
implementation of PAT approaches
Final Thoughts
27 |
Upstream Process Development
Brian Baker
Venkata Tayi
Niket Bubna
Cameron Phillips
Jingshu Zhu
Acknowledgements
28 |
Analytical Development
James Smedley
Nate Oien
Derek Ryan
Management
Abhinav Shukla
Tim Kelly
Prathima Acharya
Joe McMahon