j-module 1.2 preparation (cmc): model document for ... culture fluid total culture days (pca)...
TRANSCRIPT
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J-Module 1.2 Preparation
(CMC): Model Document for
Manufacturing Process
Description
JPMA Biopharmaceutical Committee
Technology Working committee
Kei Nishimura
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Contents
• J-Module 1.2
• Model document (Mock-up)
– Background / overview
– Example 1: Production culture
– Example 2: Affinity chromatography
• Summary
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Current
• Guideline for Descriptions on Application Forms for
Marketing Approval of Drugs, etc. under the Revised
Pharmaceutical Affairs Law” (PFSB/ELD Notification No.
0210001, dated February 10, 2005)
• Study about impact of manufacturing process for bio-
products on the quality – Introduction of minor change
notification (Module 1.2 of bio-products) – (Toru
Kawanishi 2006)
• ICH Guidelines Q9, Q10, Q11 (2006, 2010, 2014)
• Lots of Bio-product approved
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Structure of J-module 1.2
• Product Name
• Ingredient and Contents
• Manufacturing Process
• Dosage and Administration
• Indications
• Storage and Shelf life
• Specification and Testing Method
• Manufacturing Sites
・・・・・・・・・・・・・・・
Legally-binding
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• Evaluation results
– Process evaluation
– Validation
– CQA evaluation
– Risk evaluation
– Control strategy
etc.
• Controls under GMP
– Raw material/labeling and packaging material
– Process
– Parameter
– Process control
– In-process control
etc.
Approval matters【Manufacturing process】
• Notice
• Review:
Inquiries
Information to support
manufacturing process section
• Module 3
• Module 2.3
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Manufacturing process section
Information to be covered
• Preparation of gene expression constructs
• Preparation and control of MCBs
• Preparation and control of WCBs
• Manufacturing of drug substances
– Culture process and purification process
• Manufacturing of drug products
• Raw materials
• Manufacturing sites
• Manufacturing process flow chart
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Change controls in manufacturing
process• Changes of manufacturing process should be
addressed by Partial Change Application (PCA) in principle.
• A Minor Change Notification (MCN) may be applicable. Ex. Acceptable range
• Manufacturing process column should clarify change procedure MCN/PCA.
≪ XX ≫:Target/Set Value. Should be changed by PCA
『 XX 』: Target/Set Value. MCN is applicable.
“○○○”:MCN is applicable
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Mock-up (draft)
• JPMA Biopharmaceutical Committee
Technology Working committee prepares
specific description examples (Mock-up)
for the drug substance manufacturing
process section for general antibody
drugs.
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Points to consider
• Guideline for Descriptions on Application Forms for
Marketing Approval of Drugs, etc. under the Revised
Pharmaceutical Affairs Law” (PFSB/ELD Notification No.
0210001, dated February 10, 2005)
• Study about impact of manufacturing process for bio-
products on the quality – Introduction of minor change
notification (Module 1.2 of bio-products) – (Toru
Kawanishi 2006)
• ICH Guidelines Q9, Q10, Q11 (2006, 2010, 2014)
• Company experience
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Mock-up preparation process
• Based on J-module 1.2s and past application experiences
of the committee members, items (e.g. parameters) were
divided into two groups (included in J-module 1.2, and
not included). Then the individual items were reviewed
and reflected to the Mock-up.
# Process Critical
process
Param
eter
Assess
ment 1
Assess
ment 2
Mock
up
Examp
le
In-process
control
Reason
1-1) Seed
culture
No Scale Y/N Y N 0.0003
m3
Cell density …
Media Y Y Y
Amou
nt of
media
Y/N N N 100mL
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Mock-up draft for bioproducts
• Each process has various process parameters and in-
process control tests. For this reason, an individual
approach should be taken to prepare J-Module 1.2 by
taking into account of assessment (e.g. process
evaluation, validation, CQA evaluation, risk evaluation
and control strategies ).
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Antibody Drug (model)
• Antibody-producing cells: CHO/DG44
• Antibody class:IgG
• Non-sterile drug substance
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Manufacturing process overview
• Production culture
scale: 15000 L
(volume)
• Media: Serum-free
medium
• Culture process yield:
approx. 3 g/L
• Purification process
yield: 50%
WCB
Seed culture
Expansion culture
Production culture
Harvest
Anion Exchange
Chromatography
Affinity
Chromatography
Caution Exchange
Chromatography
Low-pH virus
inactivation
Virus filtration
UF / DF
Drug
substance
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Production culture: General picture
• Purpose: cell proliferation, production of desired
antibodies
• Culture vessel: SUS fermenter or single-use
bioreactor
• Add medium to production culture only once.
• Add a specified medium for nutrient supplement
at a specified day.
• Specified as a critical step.
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Culture process: Production cultureThe expansion culture fluid is used to inoculate a culture vessel (with a capacity of 15000 L) containing ≪7000 L≫ of Medium 3 to a viable cell density of ≪1 ×105 cells/mL≫ and cultured at ≪37°C≫ and ≪pH○≫.
After ◊ days of culture, the culture is fed with ≪3000 L≫ of Medium 3 and further cultured at ≪37°C≫ and ≪pH○≫.
After ♦ days of culture, the culture is fed with glucose solution to a final concentration of ≪□ g/L≫ and production culture is continued for a total of ≪X days≫.
In-process control test:
Bioburden: < ○○ CFU/mL
Adventitious virus: no evidence of viral contamination
Mycoplasma: negative
Media pH Components
Medium 3 ■ Glucose ≪A g/L≫, Fatty acids ≪B
g/L≫, Synthetic IGF-1 ≪C g/L≫, ---
Glucose solution
(supplement medium)
- Glucose ≪ε g/L≫
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Production culture: Information to be described
(proposal)
Culture
fluid
Culture vessel
MediaMedium components
(PCA)
Viable cell viability (description
omitted)
Capacity (PCA)
Medium addition volume
(PCA) Target viable cell density
(PCA)
Culture conditions
Dissolved CO2 level, Dissolved
oxygen concentration (DOC),
Osmotic pressure, Agitation
speed, Vessel internal pressure,
Aeration rate (description
omitted)
Initiation of the
culture
Temperature/pH (PCA)
Final cell viability is ensured
when a specific culture
condition is established.
These parameters should be
described if they pose a high
risk based on risk assessment.
Final cell viability is ensured
when a specific culture
condition is established.
* PCA: Partial Change Application
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Production culture: Information to be described
(proposal)
Initiation of culture
Monitoring
Residual nutrient component level,
and metabolite level (descriptions
omitted)
Medium addition
Timing of medium
addition (PCA)
Medium
Amount of medium addition (PCA)
The process was validated;
changes are not expected
unless abnormalities occur.
Culture conditions
MonitoringResidual nutrient component
level, and metabolite level
(descriptions omitted)
Dissolved CO2 level, Dissolved
oxygen concentration (DOC),
Osmotic pressure, agitation speed,
Vessel internal pressure, Aeration
rate (description omitted)
Addition of
supplement medium
Timing of culture
addition (PCA)
Composition of medium (PCA)
Target final concentration (PCA)
Temperature/pH (PCA)
Supplement
medium
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Production culture: Information to be described
(proposal)
Addition of supplement
medium
Culture conditions
Monitoring Residual nutrient component
level, and metabolite level
(description omitted)
Dissolved CO2 level, Dissolved oxygen
concentration (DOC), Osmotic
pressure, agitation speed, Vessel
internal pressure, Aeration rate
(description omitted)
Temperature/pH
(PCA)
Production
culture fluid
Total culture days
(PCA)
Maximum number of population doublings, Viable cell
density (final) , Cell viability (final), Cell productivity, Cell
production volume, Purity (description omitted)
Based on validation data.
Endotoxin (description omitted)Endotoxin test is clarified in the drug
substance specifications and test methods.
Bioburden, Adventitious virus, Mycoplasma (PCA)
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Affinity chromatography process:
General picture
• Purpose: Purity improvement, Remove raw materials/process-related impurities/HCP
• Protein A column is used.
• Precolumn is not used.
• The entire amount of fluid obtained from the previous process is loaded.
• No critical intermediates to be isolated and held.
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Purification process: Affinity
chromatography1) Affinity chromatography
The harvested culture fluid is loaded onto an affinity column packed with 『X
L』 of resin (PRODUCT NAME or equivalent) to allow adsorption of desired
antibody. The column is washed with Buffer A, followed by elution with Buffer B at a flow rate of 『○○ cm/h』. With the absorbance monitored at 280 nm, the
fraction containing desired antibody is pooled (start of pooling at OD280
『○○』; end of pooling 『××』) to obtain the eluate pool.
Buffer Components pH
Buffer A Tris 『×× mol/L』, --- -
Buffer B Sodium acetate ≪×× mol/L≫, --- 『6.5』
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Affinity chromatography: Information
to be described (proposal)
Column Column material/resin, and size (PCA)
Equilibration
Composition of buffers
(description omitted)
The maximum number of column reuse will not
be described, on the premise that its change is
subject to control under GMP.
Number of column reuse (description omitted
In principle, appropriate conditions may be set according
to the column characteristics and controlled under GMP.
Equilibration buffer
Amount of buffer fluids to be run or
loaded (description omitted).
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Affinity chromatography: Information
to be described (proposal)Harvested
culture fluid
Column
Washing
Elution
Evaluation results showed that the
acceptable range for flow rates is wide,
and it is not allowed to run the upper
limit of the column pressure.
Flow rate (omitted)
In principle, appropriate conditions
may be set according to the
column characteristics and
controlled under GMP.
Load volume
(description omitted)
As the entire amount of process
fluid is loaded.
Washing bufferComposition of buffers
(PCA/MCN)
Amount of buffer to be run (description omitted).
PCA: Partial Change Application
MCN: Minor Change Notification
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Description items relating to the affinity
chromatography
Elution Elution buffer Composition of buffers
(PCA/MCN)
The flow rate and the range of pooling (MCN)
pH, conductivity (descriptions omitted)
It was assumed that study results identified the
flow rate and the range of pooling as process
parameters of this stepFraction
Column
Storage Regeneration buffer Composition of buffers
(descriptions omitted)
In principle, appropriate conditions may be set according
to the column characteristics and controlled under GMP.
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Summary
• The current status on the J-Module 1.2 application (legal binding part) is
mainly to be prepared by the company experience and policy, in
addition to the previous reference proposed in 2006.
• Recently due to the detailed description in J-M1.2 previously, it
increases the prior to approval matters and then increase the supply risk.
• In order to reduce the change control items with the essential items in J-
M1.2, JPMA is under preparing the Mock-up draft with describing more
necessary legal binding information for the approval.
• At present, JPMA approach is focused on the draft preparation for the
manufacturing process of drug substance, reflecting the risk evaluation
information from the process evaluation/process validation results until
now.
• JPMA will start the discussions on the Mock-up preparation with PMDA
near future.