process development & gmp production of pfama1 …€¦ · process development & gmp...
TRANSCRIPT
EVI rendez-vousNov. 14th, 2011
Stephan Hellwig
Process development &GMP production of
pfAma1 DiCo1-3 clinical-grade API
Efficient project communication among 3-5 partners fromdifferent countries was achieved by ca. 60-80 Teleconferences and only ca. 5 face-to-face meetings
Cell separation and FiltrationFollowing High-cell-density Pichia
fermentation
Downstream processing of the API in class C cleanrooms
Release testing of the API or purified bulk
What‘s behind the phone ?1 batch of each pfAma1 DiCo API was
produced in accordance with GMP andfilled in aliquots for further processing.
Project progress12-2008: First contact
01-2009: Quotation WP 1 (Non-GMP PD)
06-2009: Contract signed
07-2009: First fermentation
02-2010: Audit NNE Pharmaplan
04-2010: Manuf. & qualif. of MCBPreparation of Manuf. Instruction
06-2010: Finalization of WP 1 (Non-GMP)
06-2010: First technical run in cleanroomFinalizing Manuf. Instruction
08-2010: GMP contract signed
11-2010: GMP campaign (4 weeks)
Until now: Release QCFormulation developmentDP manufacturing
Process developmentProcess development
The infamous degradations
-0,4
-0,2
0
0,2
0,4
0,6
0,8
1
1,2
1,4
0,0000001 0,000001 0,00001 0,0001 0,001 0,01
E40
5
1/Dilution
Supernatants PPF 122, est. ca. 90 mg/L in harvest supernatant
SN122-4
SN122-5
SN122-8
SN122-7
SN-122-8
SN122-9
SN122-10
SN122-11
STandard
Early & Final fermentation protocols –trading off yield for quality
0 12 24 36 48 600
20
40
60
80
1000
500
1000
1500
Dis
solv
ed o
xyge
n [%
]Te
mpe
ratu
re [°
C]
Time [h]
StartMeOH feed
StartGY feed
50%
w/v
Gly
cero
l Fee
d +
Ptm
1 [m
L]M
eOH
feed
+ P
tm1
[mL]
12.5
% N
H4O
H [m
L]
0
50
100
150
200
250
300
350
baseFW
OD
600,
FW [g
·L-1]OD
5,50
5,75
6,00
6,25
6,50
PPF 109 AMVAC_01_ND1_20 L
pH
0 12 24 36 48 600
50
100
150
2000
150
300
450
600
750
900
Dis
solv
ed o
xyge
n [%
]Te
mpe
ratu
re [°
C]
Time [h]
StartMeOH feed
StartGY feed
50%
w/v
Gly
cero
l Fee
d +
Ptm
1 [m
L]M
eOH
Fee
d +
Ptm
1 [m
L]25
% N
H4O
H [m
L]
0
50
100
150
200
250O
D60
0
FW
[g·L
-1]Base
FW
OD
5,50
5,75
6,00
6,25
6,50
PPF 134 AMVAC_01_ND3_20 L
pH
Media comparison
Component Invitrogen 1st gen. IMEPhosphoric acid (85 %)
23.7 mL 23.87 mL 4.25 mL
CaSO4∙2H2O 1.18 g 1.05 g 0.18 gK2SO4 18.2 g 18.28 g 2,81 g MgSO4 7H2O 14.9 g 14.96 g 2.31gKOH 4.13 g 4.15 g 0.72Glycerol (1.26 g/mL) 40 g 40.17 g 50 mLEDTA 0 g 0.150 g 0.150 gPtm1 Trace salts 4.35 mL 4.76 mL 4 mL
Component Invitrogen 1st. gen (Low Cu) IME
CuSO4∙5H2O 6.0 g 0.6 g 0.6 gNaI 0.08 g 0.08 g 0.08 gMnSO4∙H2O 3.0 g 3.0 g 3.0 gNa2MoO4∙2H2O 0.2 g 0.2g 0.2 gBoric acid 0.02 g 0.02 g 0.02 gCoCl2∙6H2O 0.5 g 0.92 g 0.2 gZnCl2 20 g 20 g 20 gFeSO4∙7H2O 65 g 65 g 65 gBiotin 0.2 g 0.2 g 0.2 gH2SO4 conc. 5 mL 5 mL 5 mL
Stability after IMAC 1 – determining hold steps
N-terminal alternatives
Gradient‐Elution HIC
Coloration in Ama1 DiCo DSP
1st generation vaccine process history report describes that :• Butyl-eluate still contained Pichia pigments but in a less extent than IMAC-eluate. Butylchromatography was thus kept as second purification step.
IME made the very same observation, but recommendation from QA and QP is to investigate the nature of the contaminant or to remove it
Coloration in Ama1 DiCo DSP
Lots of experiments to get rid of colouration Is the protein brownish ?
Early (non-GMP) purified bulk stability
Looking into the future at an early point in development: stability of formulated
lyophilized purified bulk
Scaleup & Transfer to GMP
Scaleup & Adaption to GMP
Total processing time: ca. 6‐8 hoursTotal work day: ca. 8‐12 hours
Temperature issues duringprocessing ?
Disposables cost approx. 850 €bags, ca. 800 € filters
Possible layout of cell separation
CARR
product
filtrate1,5 µm
Filter1,5 µm
bulkharvest
Filter0,22 µm
Carrcentrate
08.09.2010, ca. 24 h, ca. 2/3 of bulk harvest processed
Post manufacturing of drug substance
Release testing issues
• DiCo‐specific assay to quantify each API in the mix:• DiCo‐specific ELISA• RP‐HPLC• BiaCore
• Host‐cell proteins• Commercially available „Cygnus“‐Kit not useful (cross‐reactivity)
• Dimers & Aggregates
Drug substance formulation development: Analysis of aggregates and dimers
Drug substance to drug product: Formulation & Lyophilization
• Aggregates occurduringlyophilization
• Dimers occur, time‐dependantand possiblyoxygen‐dependant in PP vials, but not in EVA bags.