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FDA’s GMP Inspection with
special regard to Aseptic
Process for Drugs & Biologicals
Professor Chung Keel Lee, Ph.D.
Special Advisor to the Minister, MFDS
Invited Professor, EWU & SNU
Advisor to World Health Organization(WHO)
Chair, Korea Affiliate, International Society for
Pharmaceutical Engineering(ISPE)
March 22, 2018
Gyeongin Regional Office of MFDS
Thecountries visitedbyCKLasaninspector and/ortrainer
since1987
2
Argentina Chile Denmark Korea Myanmar Taiwan Venezuela
Australia China Indonesia Malaysia Philippines Thailand Vietnam
Brazil Colombia Iran Mexico Russia USA
Bulgaria Cuba Japan Mongolia Singapore Uzbekistan
Contents
• Four Basic Elements of CGMP : “4Ms”
• System-based Inspection
• Latest GMP Trends(QbD)
• Sterile Drug Products Produced by Aseptic
Processing
• Significant Deficiencies by System-based
Inspection
• Question & Answer Session
Four Basic Elements of CGMP
“4Ms”
Men Machinery
Materials Methods
Qualification
Adequate training
Products
Reagents
Components
Containers & Closures
Labels
Manufacturing
Control
Validation
Documentation
Buildings
Facilities
Equipment
Tools
 “4Ms”
 Men
• Organization : Independence
• Qualification
• Training
• Personnel Responsibilities
Four Basic Elements of CGMP
 Materials
• Receipt
• Sampling
• Testing
• Release
• Retesting
• Cell Banking
• Viral Seeds
• Reagents
• Labels
• Products
Untested Components,
Drug product Containers
& Closures
Four Basic Elements of CGMP
 Machinery
• Building Design
• HVAC System
• Water For Injection
System
• Clean Steam System
• Washing & Toilet
Facilities
• Laminar Flow Hoods.
HEPA
filter
Four Basic Elements of CGMP
FDA
Descriptive Class 100 Class 10,000 Class 100,000 ND
In Operation
≥ 0.5㎛
/ft3 100 10,000 100,000 ND
Action
Level
CFU/m3
1 10 100 ND
EU,
WHO,
PIC/S
Descriptive A B C D ND
At Rest
≥ 0.5㎛
/m3 3,520 3,520 352,000 3,520,000
≥ 5㎛
/m3 20 29 2,900 29,000
In Operation
≥ 0.5㎛
/m3 3,520 352,000 3,520,000 ND
≥ 5㎛
/m3 20 2,900 29,000 ND
CFU/m3 < 1 < 10 < 100 < 200
ISPE Descriptive Grade 5 Grade 7 Grade 8 CNC+ CNC
ISO
Descriptive ISO. 5 ISO. 7 ISO. 8 ISO. 9
In Operation
≥ 0.5㎛
/m3 3,520 352,000 3,520,000 35,200,000
≥ 5㎛
/m3 20 2,930 29,300 293,000
Comparison of Air Cleanliness Classifications
 As-Built condition
- Where the installation is complete with all services
connected and functioning but with no equipment
& personnel present.
 At-Rest condition
- Where the installation is complete with equipment
installed and operating but with no personnel
present.
 Operational condition
- Where the installation is functioning with the
specified No. of personnel present & equipment
operating.
3 Occupancy States
 Methods
• Production
• Sampling & Testing
• Environmental Monitoring
• Packaging & Labeling
• Validation
• Documentation
• Storage
Drug Products
Release
Quality Control(QC)
- Under appropriate conditions
Quarantine
- The oldest stock product
is distributed first
- A system to readily determine
the distribution of drug
Four Basic Elements of CGMP
 Quality System
 Facility & Equipment
 Materials
 Production
 Laboratory Controls
 Packaging & Labeling
System Based Inspection
CGMP Subpart Qual. F/E Mat. Prod PKG/L Lab.
B. Organization & Personnel      
C. Buildings & Facilities 
D. Equipment 
E. Control of Components & Drug Product
containers & closures
 
F. Production & Process Controls  
G. Packaging & Labeling Control  
H. Holding & Distribution 
I. Laboratory Controls  
J. Records & Reports      
K. Returned & Salvaged Drug Products  
CGMP vs. Systems
 Introduction
 2002 : Pharmaceutical CGMP Initiative for
the 21st Century-A Risk Based Approach
The Pharmaceutical Quality for the
21st Century-A Risk Based Approach
Latest GMP Trends(QbD)
Research & Development
Commercial
Manufacturing
Post-market
Surveillance
Pre-clinical
Clinical
Ⅰ Ⅱ Ⅲ
Risk-based Approach
Quality System Approach
Traditional
Enhanced
The entire lifecycle of a product
Latest GMP Trends(QbD)
 Traditional vs. New Enhanced Approach
 QTPP
 CQA of the product
 Input variables : materials etc.
 Process parameters : temp., time, humidity etc.
 Multidimensional combination & interaction → Design Space
 Real time release (test)
 Quality by Design → Regulatory flexibility
Latest GMP Trends(QbD)
 Ishikawa (Fishbone) Diagram (risk assessment tool)
 US FDA’s Guidances with Enhanced Approach (QbD)
 Sterile Drug Products Produced by Aseptic Processing –CGMP
(Sept., 2004)
 Process Analytical Technology (PAT) : A Framework for
Innovative Pharmaceutical Development, Manufacturing &
Quality Assurance (Sept., 2004)
 Quality Systems Approach to Pharmaceutical CGMP Regulations
(Sept., 2006)
 Process Validation : General Principles & Practices (Jan., 2011)
Latest GMP Trends
 ICH Harmonized Tripartite Guidelines
 Pharmaceutical Development (ICH Q8:R2) (Aug., 2009)
 Quality Risk Management (ICH Q9) (Nov., 2005)
 Pharmaceutical Quality System (ICH Q10) (June, 2008)
 Development & Manufacture of Drug Substances (ICH Q11)
(Nov., 2012)
Latest GMP Trends
Sterile Drug Products produced
by Aseptic Processing
I. Introduction
II. Background
III. Scope
IV. Building & Facilities
V. Personnel Training
VI. Components &
Containers/Closures
VII. Endotoxin Control
VIII. Time Limitations
IX. Validation of Aseptic
Processing & Sterilization
X. Laboratory Controls
XI. Sterility Testing
XII. Batch Record Review
I. Introduction
• Replacement of 1987 guideline on sterile
drug products produced by aseptic
processing (aseptic processing guideline)
• When manufacturing sterile drug and
biological products using aseptic processing
II . Background
A. Regulatory Framework
 Where it is impossible to comply with the
applicable regulations in both parts 600
through 680 and parts 210 & 211, the
regulation specifically applicable to the drug
product in question shall supercede the
more general regulations.
III. Scope
• This guidance updates the 1987 Aseptic
Processing Guideline with respect to:
– personnel qualification
– cleanroom design
– process design
– quality control
– environmental monitoring
– review of production records
IV. Buildings and Facilities
• Clean area air classifications: measured
at work level under dynamic conditions
* You may establish alternate levels due to the nature of the operation or method of analysis.
** Normally yield no microbiological contaminants.
Clean Area
Classification
(≥ 0.5 mm
particles/ft3)
ISO
Designation
> 0.5 mm
particles/m3
*CFU/m3
(active S.)
*CFU/4-hr
(passive S.
diam. 90mm)
100 5 3,520 <1** <1
1000 6 35,200 <7 <3
10,000 7 352,000 <10 <5
100,000 8 3,520,000 <100 <50
IV. Buildings and Facilities
A. Critical Area-Class 100 (ISO 5)
 A critical area is one in which the sterilized
drug product, containers, and closures are
exposed to environmental conditions that
must be designed to maintain product sterility.
 Particles:
– Extraneous contaminant themselves
– Act as a vehicle for microorganisms.
– To be measured not more than 1 foot away from
the work site.
– Regular monitoring should be performed during
each production shift.
IV. Buildings and Facilities
A. Critical Area-Class 100 (ISO 5)
 High levels of product particles
– Qualification of the area under dynamic conditions
without actual filling function
 In situ air pattern under dynamic conditions
– Unidirectional air flow
– Sweeping action over & away from the product
• A velocity of 0.45 meters/second (90
feet/minute) ±20%
IV. Buildings and Facilities
B. Supporting Clean Areas
 To be designed to minimize the level of particle
contaminants & microbiological content (bioburden)
 The area immediately adjacent to the aseptic
processing line should meet, at a minimum, class
10,000 (ISO 7) standards under dynamic conditions.
Class 1,000 (ISO 6) or Class 100 may apply to this
area.
 Class 100,000 (ISO 8) air cleanliness level is
appropriate for less critical activities (e.g.,
equipment cleaning).
IV. Buildings and Facilities
C. Clean Area Separation
 Airflow from higher cleanliness area to
adjacent less clean areas.
 A substantial positive pressure differentials
for rooms of higher air cleanliness
 10-15 Pa (0.04-0.06 inches of water gauge )
maintained between rooms of differing
classification with doors closed.
IV. Buildings and Facilities
C. Clean Area Separation
 At least 12.5 Pa should be maintained
between the aseptic processing room and
unclassified room adjacent to the aseptic
processing room.
 Pressure differentials should be monitored
continuously & frequently recorded.
IV. Buildings and Facilities
C. Clean Area Separation
• For class 100,000 (ISO 8) at least 20 air
changes per hour is acceptable.
Significantly higher air change rates are
normally needed for class 10,000 & Class
100 areas.
• A suitable facility monitoring system (i.e.,
alarms) is needed.
IV. Buildings and Facilities
D. Air Filtration
1. Membrane
 Membrane filters (sterile) can be used for
compressed gas, autoclave air lines, lyophilizer
vacuum breaks, tanks containing sterilized materials.
 Gas filters (including vent filters) should be dry.
 Filters that supply sterile gases should be integrity
tested upon installation & periodically thereafter (e.g.,
end of use).
IV. Buildings and Facilities
D. Air Filtration
2. HEPA
• Leak testing at installation
• 2 x / year for aseptic processing room
• Facility renovation, media fill failure, drug product
sterility failure... : additional testing
• Leak test on dry heat depyrogenation tunnels &
ovens(e.g. glass vials)
IV. Buildings and Facilities
D. Air Filtration
2. HEPA
• DOP (DiOctylPhthalate) or PAO (Poly-Alpha-Olefin)
– Leak testing aerosols
• Alternative aerosols
– Not promoting microbial growth
• Filter efficiency test
– Monodispersed aerosol of 0.3μ particles
– Retaining at least 99.97%
IV. Buildings and Facilities
D. Air Filtration
2. HEPA
 Filter Integrity test
– Polydispersed aerosol (mean < 1μ but > 0.3 μ)
– Sufficient No. of particles at ~0.3μ.
– Test in place
– Scan at 1~2 inches from the filter face
– Sampling rate at ≥1 ft3/min.
– > 99.99% retention or < 0.01% leak
• Uniformity of velocity across the filter
– Variations in velocity can cause turbulence.
– Velocity of unidirectional air
» At 6 inches from the filter face and
» At work level in critical area
IV. Buildings and Facilities
E. Design
• Aseptic processes designed to minimize
exposure of sterile articles to contamination
hazards
• Flow of personnel, materials, products,
equipment, air & waste
• Minimum No. of personnel in aseptic
processing area
• SIP (sterilize-in-place) or automation of
processes can reduce risk to the product.
IV. Buildings and Facilities
E. Design
• A partially closed sterile product should be
transferred only in critical areas.
– The area between a filling line & the lyophilizer
• Appropriately designed transfer equipment can be
qualified for this purpose.
• Airlocks with interlocking doors between aseptic
processing area entrance and unclassified area.
• Stoppered vials should be under protection until
completion of the crimping step.
IV. Buildings and Facilities
E. Design
• Seamless & rounded floor to wall junctions,
readily accessible corners…
• Sanitary fittings & valves for processing
equipment
• No drains in aseptic processing areas
• Avoid horizonal surfaces or ledges
• SOPs on returning a facility to operating
conditions following a shutdown
V. Personnel Training
A. Personnel
• Evaluate each operator’s conformance to
written procedures during operation.
• QC’s regular oversight on adherence to
established, written procedures during
manufacturing
• Techniques to maintain sterility of sterile
items & surfaces:
– Contact sterile materials only with sterile
instruments.
– Move slowly and deliberately.
V. Personnel Training
A. Personnel
• Techniques to maintain sterility of sterile
items & surfaces:
– Keep the entire body out of the path of
unidirectional airflow.
– Approach from the side & not above the
production in vertical laminar flow.
– Refrain from speaking when in direct proximity to
the critical area.
– Maintain proper gown control.
V. Personnel Training
A. Personnel
 Gowns: sterile, nonshedding, covering the skin &
hair
– Common elements of gowns: face-masks, hoods,
beard/moustache covers, protective goggles
– Adequate barrier should be created by the
overlapping of gown components.
– Gloves should be sanitized frequently.
• Microbiological surface sampling of several
locations on gown : e.g., glove fingers, facemask,
forearms, chest etc.
V. Personnel Training
A. Personnel
• Periodic requalification following an initial
assessment of gowning
• Annual requalification for automated
operations
B. Laboratory Personnel
• The basic principles of training, aseptic
technique, and personnel qualification in
aseptic manufacturing also are applicable to
those performing aseptic sampling and
microbiological laboratory analyses.
V. Personnel Training
C. Monitoring Program
 Obtain surface samples of each operator's gown
including gloves & other locations of the gown on a
daily basis, or in association with each lot.
 Asepsis is fundamental to an aseptic processing
operation.
 Sanitizing gloves just prior to sampling is
inappropriate because it can prevent recovery of
microorganisms that were present during an aseptic
manipulation.
VI. Components and
Container/Closures
A. Components
 Active ingredients, water for injection (WFI),
and other excipients: acceptable limits of
microbial content (e.g., bioburden, endotoxin)
should be established.
 Sterile-filtration of a solution formed by
dissolving the component (s) in a solvent such
as WFI, USP, is used when the solution is
adversely affected by heat.
VI. Components and
Container/Closures
A. Components
 Dry heat sterilization is good for components
that are heat stable and insoluble. Heat
penetration & distribution studies are
needed for powder sterilization because of
the insulating effects of the powder.
 Irradiation can be used to sterilize some
components.
VI. Components and
Container/Closures
B. Containers/Closures
1. Preparation
• Containers & closures should be sterile and, for
parenteral drug nonpyrogenic.
• Time limits for holding sterile & depyrogenated
containers & closures
• Final rinse water should be purified water and,
for parenteral products WFI, USP.
• Subjecting glass containers to dry heat
accomplishes both sterilization & depyrogenation.
VI. Components and
Container/Closures
B. Containers/Closures
1. Preparation
• Ethylene oxide (EtO) : effective surface sterilant
– Temperature, pressure, humidity, gas
concentration, exposure time, degassing,
aeration, & residuals should be specified &
monitored.
– Biological indicators are of special importance in
demonstrating the effectiveness of EtO & other
gas sterilization processes.
• Rubber closures (e.g., stoppers and syringe
plungers) :
– Multiple cycles of washing / rinsing prior to sterilization
VI. Components and
Container/Closures
B. Containers/Closures
1. Preparation
• Rubber closures (e.g., stoppers and syringe plungers) :
– Initial rinses with PW, USP followed by
– Final rinse with WFI, USP for parenteral products
– Depyrogenation by multiple rinses of hot WFI
– The time between washing / drying and sterilizing should be
minimized.
– Siliconization of rubber stoppers: potential sources of
contamination
• Visual identification & Certificate of Analysis review on
containers & closures may be accepted with the reliability
of the supplier’s test results established at appropriate
intervals.
VII. Endotoxin Control
• Endotoxin contamination of an injectable
product can occur as a result of poor CGMP
controls.
• Drug product components, containers,
closures, storage time limitations, and
manufacturing equipment are among the areas
to address in establishing endotoxin control.
• Adequate cleaning, drying, and storage of
equipment will control bioburden and prevent
contribution of endotoxin load.
VII. Endotoxin Control
• Sterilizing-grade filters and moist heat
sterilization have not been shown to be
effective in removing endotoxin.
• Some clean-in-place procedures employ initial
rinses with appropriate high purity water and/or
a cleaning agent (e.g., acid, base, surfactant),
followed by final rinses with heated WFI.
• Equipment should be dried following cleaning,
unless the equipment proceeds immediately to
the sterilization step.
VIII. Time Limitations
• Time limits for each phase of aseptic processing
– Between the start of bulk product compounding and
its sterilization filtration
– Product exposure while on the processing line
– Storage of sterilized equipment, containers & closures
• Bioburden & endotoxin load should be assessed to
establish time limits for stages.
• The total time for product filtration should be limited
to an established maximum:
– To prevent microorganisms from penetrating the filter
– To prevent an increase in upstream bioburden &
endotoxin load
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
 An aseptic processing operation should be
validated using a microbiological growth medium in
place of the product. This ”process simulation”
(media fill) includes exposing the microbiological
growth medium to product contact surfaces of
equipment, container closure systems, critical
environments, and process manipulations to closely
simulate the same exposure that the product itself
will undergo during actual operations (e.g., start-up,
sterile ingredient additions, aseptic connections,
filling, closing).
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
• Aseptic processing validation:
– Microbial growth medium
– Process simulation (media fill)
– Exposure to product contact surfaces
– The sealed containers filled with the medium are incubated.
– Results are interpreted to assess the potential for a unit of
drug product to become contaminated during actual
operations.
– Environmental monitoring data from the process simulation
can also provide useful information for the processing line
evaluation
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
1. Study Design for Media Fill
a. Consider the following issues: simulate actual
operations + worst-case conditions
 Factors associated with the longest permitted run:
e.g., operator fatigue
 normal interventions & nonroutine interventions
(stoppages, equipment adjustments)
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
1. Study Design for Media Fill
a. Consider the following issues: simulate actual operations
+ worst-case conditions
 Lyophilization, when applicable
 Aseptic assembly of equipment
(e.g., at start-up, during processing)
 Number of personnel and their activities
 Representative number of aseptic additions or transfers
 Shift changes, breaks, and gown changes
(when applicable)
 Type of aseptic equipment disconnections/connections
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
1. Study Design for Media Fill
a. Consider the following issues: simulate actual
operations + worst-case conditions
 Aseptic sample collections
 Line speed & configuration
 Weight checks
 Container closure systems (e.g., sizes, type)
b. A written batch record should be prepared for
each media fill run.
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
2. Frequency and Number of Runs
 At least 3 consecutive separate successful runs should
be performed during initial line qualification.
 Subsequently, routine semi-annual qualification
conducted for each processing line will evaluate the state
of control of the aseptic process.
 All personnel authorized to enter the aseptic processing
room during manufacturing (i.e., technicians,
maintenance personnel…) should participate in a media
fill at least once a year.
 Facility & equipment modifications, line configuration
changes, significant changes in personnel, anomalies in
environmental testing results, container closure system
changes, extended shutdowns, or end product sterility
testing showing contaminated products may be cause for
revalidation of the system.
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
3. Duration of runs
 When aseptic processing employs manual filling or
closing, or extensive manual manipulations, the
duration of the process simulation should be no less
than the length of the actual manufacturing process
to best simulate contamination risks posed by
operators.
 For lyophilization operations FDA recommends that
unsealed containers be exposed to partial
evacuation of the chamber but the vials should not
be frozen & the medium should remain in an
aerobic state.
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
4. Size of runs
• 5,000 to 10,000 units
• Maximum batch size if the run size is under
5,000
• Full or close to full batch size for manually
intensive filling
• Lower number of units in case of using an
isolator due to the lack of direct human
intervention.
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
5. Line Speed
 Each media fill run should evaluate a
single line speed, and the speed chosen
should be justified.
6. Environmental Condition
 Media fills should be adequately
representative of the conditions under
which actual manufacturing operations
are conducted.
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
7. Media
• “soybean casein digest medium” in general
• Growth promotion test : e.g., USP indicator organisms
– Gram-positive & gram-negative bacteria
– Yeast
– Mold
• Substituted challenge : isolates from E.M. & sterility test
• <100 CFU challenge/unit
 Each unit should be filled with an appropriate quantity of
microbial growth medium to contact the inner container/
closure surfaces (the unit is inverted or swirled).
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
8. Incubation & Examination of Media-Filled
Units
• 20-30 ℃ ± 2.5℃
• Not less than 14 days
• If two temperatures are used:
– ≥ 7 days at 20-25 ℃, first
– ≥ 7 days at 30-35 ℃, second
• QC unit’s involvement
– Observation or
– Oversight throughout the examination
• All suspect units should be brought to QC
microbiologist.
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
8. Incubation & Examination of Media-Filled
Units
• Clear containers for amber or opaque containers
• All integral units → incubation
• Units not related to integrity (cosmetic defect) →
incubation
• Units that lack integrity should be rejected.
• Criteria for yield ( total units incubated / total
units filled)
IX. Validation of Aseptic
Processing and Sterilization
A. Process Simulations
9. Interpretation of Test Results
 The process simulation run should be observed by
the QC Unit.
 Contaminated units should be reconcilable with the
approximate time and the activity being simulated
during the media fill.
 Any contaminated unit should be identified to species
level.
 Any failure investigation should assess the impact on
commercial drugs produced on the line since the last
media fill.
 Modern aseptic processing operations should
normally yield no media fill contamination.
IX. Validation of Aseptic
Processing and Sterilization
B. Filtration Efficacy
• 0.22μ or 0.2 μ sterilization grade filters
• Sterile filtration validation:
– Microbial challenges
– Integrity test of the filters
• Brevundimonas diminuta (ATCC 19146)
• At least 107 organisms per cm2 of effective
filter area
• No passage of the challenge microorganisms
IX. Validation of Aseptic
Processing and Sterilization
B. Filtration Efficacy
• Minimize the bioburden of the unfiltered
product.
• Direct inoculation into the drug formulation is
preferred.
• Worst-case conditions : maximum filter use
time & pressure
• Filter integrity testing : before & after use
• Forward flow and bubble point tests
IX. Validation of Aseptic
Processing and Sterilization
C. Sterilization of Equipment, Containers,
and Closures
• Moist heat and dry heat sterilization
1. Qualification & Validation
• Requalification on a periodic basis
• Remove air from the autoclave chamber.
• Filter installations in piping (SIP)
– Pressure differential across the filter
– Significant temperature drop on the downstream
– Place biological indicators at downstream locations
of the filter.
IX. Validation of Aseptic
Processing and Sterilization
C. Sterilization of Equipment, Containers,
and Closures
• Moist heat and dry heat sterilization
1. Qualification and Validation
• Empty chamber studies :
– Temperature & pressure mapping study with
calibrated measurement devices
– Heat penetration studies on loading configurations
– In general, the biological indicator should be
placed adjacent to the temperature sensor to
assess the correlation between microbial lethality
and predicted lethality based on thermal input.
IX. Validation of Aseptic
Processing and Sterilization
C. Sterilization of Equipment, Containers,
and Closures
• Moist heat and dry heat sterilization
1. Qualification and Validation
 Articles difficult to sterilize: filters, filling manifolds,
pumps. Some other examples include certain locations
of tightly wrapped or densely packed supplies, securely
fastened load articles, lengthy tubing, the sterile filter
apparatus, hydrophobic filters, and stopper load.
 A sterility assurance level of 10-6 or better should be
demonstrated for a sterilization process.
IX. Validation of Aseptic
Processing and Sterilization
C. Sterilization of Equipment, Containers,
and Closures
• Moist heat and dry heat sterilization
1. Qualification and Validation
 For more information, refer to “ Guideline for the
Submission of Documentation for Sterilization Process
Validation in Applications for Human and Veterinary
Drug Products”.
 Change control procedures should adequately address
issues such as a load configuration change or a
modification of a sterilizer.
IX. Validation of Aseptic
Processing and Sterilization
C. Sterilization of Equipment, Containers, and
Closures
• Moist heat and dry heat sterilization
2. Equipment Controls & Instrument Calibration
• For both validation & routine process control, calibrate:
– Temperature & pressure monitoring devices
– Sensing devices before and after validation runs
– Devices used to monitor dwell time in the sterilizer
– D-value (resistance) of a biological indicator (e.g., spore
strips, glass ampuls) can be accepted if the reliability of a
vendor’s COA is established.
– The microbial count of a B.I.
IX. Validation of Aseptic
Processing and Sterilization
C. Sterilization of Equipment, Containers,
and Closures
• Moist heat and dry heat sterilization
2. Equipment Controls & Instrument Calibration
 For both validation & routine process control, calibrate :
- For dry heat depyrogenation tunnels, devices used
to measure belt speed should be routinely
calibrated.
- Routine evaluation of sterilizer performance-
indicating attributes, such as equilibrium (come up)
time is important in assuring that the unit continues
to operate as per the validated conditions.
X. Laboratory Controls
A. Environmental Monitoring
1. General Written Program
 In aseptic processing, one of the most important
laboratory controls is the environmental
monitoring program.
 Monitoring should cover all production shifts.
 Evaluate the quality of air & surfaces:
– Air, floors, walls, equipment surfaces (especially
critical surfaces)
– Critical surfaces : come in contact with the sterile
product, containers, & closures.
X. Laboratory Controls
A. Environmental Monitoring
1. General Written Program
 Written procedures (SOPs) should include :
– Locations to be sampled
– Sample timing ; i.e., during or at the conclusion of
operations
– Sample frequency
– Duration of sampling
– Sample size : e.g., surface area, air volume
– Sampling equipment & techniques
– Alert & action levels
– Appropriate response to deviations from alert or
action levels
X. Laboratory Controls
A. Environmental Monitoring
1. General Written Program
 Samples should be taken throughout the
classified areas of the aseptic processing facility
(e.g., aseptic corridors, gowning rooms).
 Sample sizes should be sufficient to optimize
detection of environmental contaminations at
levels that might be expected.
 Critical surface sampling should be performed at
the conclusion of the aseptic processing
operation to avoid direct contact with sterile
surfaces during processing.
X. Laboratory Controls
A. Environmental Monitoring
2. Establishing Levels & a Trending Program
 Alert & action levels
– Based on the relationship of the sampled location to the
operation
– Based on the need to maintain adequate control
– Consider E.M.data from historical databases, media fills,
clean room qualification & sanitization studies.
 QC unit should provide routine oversight of
trends in environmental & personnel monitoring
data.
– Near-term trends: daily, weekly, monthly & quarterly
– Long-term trends: yearly, biennially,….
X. Laboratory Controls
A. Environmental Monitoring
3. Disinfection Efficacy
 Disinfectants should be sterile, in suitable
containers (e.g., sterile) and used for no longer
than the predefined period .
 Routinely used disinfectants should be effective
against the normal microbial vegetative flora
recovered from the facility.
 Many common disinfectants are ineffective
against spores.
 Disinfection procedures should be described in
detail e.g., preparation, work sequence, contact
time etc.
Definitions
 Sanitization : Reduces viable microorganisms to a defined
acceptable level. Normally achieved by using a chemical agent or
heat.
 Disinfection : Process by which viable microbiological agents or
eukaryotic cells are reduced to a level unlikely to produce disease
in healthy people, plants or animals.
 Decontamination : A process that reduces contaminating
substances to a defined acceptable level
 Pasteurization : The heating of milk, wines, fruit juices, etc. for
about 30 min. at 62-68℃ whereby the living bacteria are destroyed,
but the flavor or bouquet is preserved.
 Sterilization : Destroys or eliminates all viable microbes including
bacterial spores.
Definitions (continued)
 Antiseptic : Acting against sepsis.
An antiseptic agent is one that has been
formulated for use on living
tissue(mucous membrane or skin) to
prevent or inhibit growth or action of
organisms.
 Pyrogen : A fever-producing substance called also
pyretogen, pyretic, pyrectic
Bacterial pyrogen : a fever producing
agent of bacterial origin : endotoxin
 Endotoxin : Lipopolysaccharide
Integral part of the bacterial (gram
negative) cell wall & is only released when
the integrity of the wall is disturbed.
 Depyrogenation : The removal or destruction of pyrogen
(endotoxins)
X. Laboratory Controls
A. Environmental Monitoring
4. Monitoring Methods for Biological Quality
a. Surface monitoring
 Product contact surfaces, floors, walls & equipment
 Touch plates, swabs & contact plates
b. Active air monitoring
 Active devices : impaction, centrifugal and membrane (or
gelatin) samplers
 Quantitative air monitoring
c. Passive air monitoring (settling plates)
 Settling plates: Petri dishes containing nutrient growth
medium exposed to the environment
 Qualitative, or semi-quantitative air monitoring.
 Exposure conditions should preclude desiccation (e.g.,
caused by lengthy sampling periods and/or high airflows),
which inhibits recovery of microorganisms.
A. Environmental Monitoring
5. Recommended action level of microbiological
quality (Air)
Clean Area
Classification
(0.5mm
particles/ft3)
ISO
Designation
0.5mm
particles/m3
Microbiological
Active Air
Action Levels
(CFU/m3)
Microbiological
Settling Plates
Action Levels
(diam.
90mm:cfu/4 hrs.)
100 5 3,520 1 1
1,000 6 35,200 7 3
10.000 7 352,000 10 5
100,000 8 3,520,000 100 50
US FDA, 2004 : Sterile Drug Products Produced by Aseptic Processing-CGMP
X. Laboratory Controls
A. Environmental Monitoring
6. Recommended action level of microbiological
quality (Surface)
Clean Area
Classification
(0.5mm particles/ft3)
ISO
Designation
0.5mm
particles/m3
Equipment Gloves Clothing
CFU / Contact
Plate
(24-30 cm2)
CFU / Contact
Plate
(24-30 cm2)
CFU / Contact
Plate
(24-30 cm2)
100 5 3,520 3
(including
floor)
3 5
1,000 6 35,200 – – –
10.000 7 352,000 5
10 (floor)
10 20
100,000 8 3,520,000 – – –
USP <1116>, 2006 : Microbiological Evaluation of Clean Rooms & Other Controlled Environment
X. Laboratory Controls
X. Laboratory Controls
B. Microbiological Media & Identification
• Routine identification of microorganisms to the
species levels
• Culture media capable of detecting fungi (i.e.,
yeasts and molds) & bacteria
• Total aerobic bacterial count at 30~35℃ for 48~72
hours
• Total combined yeast & mold count at 20~25℃ for
5~7 days
• Growth promotion testing on all lots of prepared
media
X. Laboratory Controls
C. Prefiltration Bioburden
• Bioburden can contribute impurities (e.g., endotoxin) to, & lead
to degradation of, the drug product.
• Minimize the bioburden in the unfiltered product.
• A prefiltration bioburden limit should be established.
D. Alternate Microbiological Test Methods :
• Rapid test methods : equivalent or better
E. Particle monitoring
• Routine particle monitoring is useful in rapidly detecting
deviations in air cleanliness.
• A result outside the established classification level at a given
location should be investigated.
 The investigation should include an evaluation of trending data.
XI. Sterility Testing
• Sterility testing lab. environment : comparable to
aseptic filling operations
• Use of isolator for sterility testing minimizes false
positive test result.
A. Microbiological Laboratory Controls
• Method validation : microbiological challenge
• If growth is inhibited :
– Increased dilution
– Additional membrane filter washes
– Addition of inactivating agents
• Media : sterile & growth promoting
• Personnel qualification & training
XI. Sterility Testing
B. Sampling & Incubation
• Limited ability to detect contamination due to
small sample size (USP):
– 10,000-unit lot with 0.1 % contamination :
20 unit sample test would pass the lot with 98% chance.
– If 10% of the lot are contaminated, contamination
can be detected about 9 out of 10 cases.
XI. Sterility Testing
B. Sampling & Incubation
 The samples should represent the entire and
processing conditions. Samples should be taken:
– At the beginning, middle, and end of the aseptic
processing operation
– In conjunction with processing interventions or
excursions
 Because of the limited sensitivity of the test, any
positive result is considered a serious CGMP issue
that should be thoroughly investigated.
XI. Sterility Testing
C. Investigation of Sterility Positives
• A positive test would be invalid only when microbial
growth can be unequivocally ascribed to laboratory
error. When available evidence is inconclusive,
batches should be rejected.
• Investigation's persuasive evidence of the origin of
the contamination should be based on :
1. Identification (speciation) of the organism in the
sterility test
 To the species level
 Determine to see the organism in lab. & production
environment
 Advanced identification method (e.g., nucleic-acid
based) are valuable for investigation.
 When comparing the results from E.M. and sterility
positives the same methodology should be used for
identifications.
XI. Sterility Testing
C. Investigation of Sterility Positives
 The investigation's persuasive evidence of the
origin of the contamination should be based on:
2. Record of Laboratory Tests & Deviation
3. Monitoring of Production area Environment :
 Trend analysis of microorganisms in the critical and
immediately adjacent areas
 Look at both short - and long - term environmental trend
analyses.
4. Monitoring Personnel
• Review of data & associated trends from daily monitoring
of personnel.
• Adequacy of personnel practices & training
XI. Sterility Testing
C. Investigation of Sterility Positives
 The investigation's persuasive evidence of
the origin of the contamination should be
based on :
5. Product Presterilization Bioburden
6. Production Record Review
 Events that could have impacted on the critical zone
 The functioning of utility and/or support systems
 Whether construction or maintenance activities could
have had an adverse impact
7. Manufacturing History
 Past deviations, problems, or changes on process,
components, equipment etc.
XII. Batch Record Review:
Process Control Documentation
• All in-process & laboratory control results
must be included in the batch production
record.
• Essential elements of the batch release
decision:
– Review of environmental & personnel monitoring
data
– Review the data relating support systems (HEPA,
HVAC, WFI, steam generator)
– Review the data on proper functioning of
equipment (e.g., batch alarms report, integrity of
various filters)
XII. Batch Record Review:
Process Control Documentation
• Interventions and/or stoppages (unplanned)
should be documented in batch records with
the associated time & duration of the event.
• Any disruption in power supply that could
affect product quality must be included in batch
production records.
Significant Deficiencies by System
A. Quality System
B. Facilities and Equipment System
C. Materials System
D. Production System
E. Packaging and Labeling System
F. Laboratory Controls System
A. Quality System
1. Pattern of failure to review/approve procedures
2. Pattern of failure to document execution of operations
as required
3. Pattern of failure to review documentation
4. Pattern of failure to conduct investigations and resolve
discrepancies/failures/deviations/complaints
5. Pattern of failure to assess other systems to assure
compliance with GMP and SOPs
Significant deficiencies by system
B. Facilities and Equipment
1. Contamination with filth, objectionable microorganisms,
toxic chemicals or other drug chemicals, or a
reasonable potential for contamination, with
demonstrated avenues of contamination, such as
airborne or through unclean equipment
2. Pattern of failure to validate cleaning procedures for
non-dedicated equipment. Lack of demonstration of
effectiveness of cleaning for dedicated equipment
3. Pattern of failure to document investigation of
discrepancies
4. Pattern of failure to establish/follow a control system for
implementing changes in the equipment
5. Pattern of failure to qualify equipment, including
computers
Significant deficiencies by system
C. Materials System
1. Release of materials for use or distribution that do not
conform to established specifications
2. Pattern of failure to conduct one specific identity test for
components
3. Pattern of failure to document investigation of
discrepancies
4. Pattern of failure to establish/follow a control system for
implementing changes in the materials handling
operations
5. Lack of validation of water systems as required
depending upon the intended use of the water
6. Lack of validation of computerized processes
Significant deficiencies by system
D. Production System
1. Pattern of failure to establish/follow a control system for
implementing changes in the production system
operations
2. Pattern of failure to document investigation of
discrepancies
3. Lack of process validation
4. Lack of validation of computerized processes
5. Pattern of incomplete or missing batch production
records
6. Pattern of nonconformance to established in-process
controls, tests, and/or specifications
Significant deficiencies by system
E. Packaging and Labeling System
1. Pattern of failure to establish/follow a control system for
implementing changes in the packaging and/or labeling
operations
2. Pattern of failure to document investigation of
discrepancies
3. Lack of validation of computerized processes
4. Lack of control of packaging and labeling operations
that may introduce a potential for mislabeling
5. Lack of packaging validation.
Significant deficiencies by system
F. Laboratory Controls System
1. Pattern of failure to establish/follow a control system for
implementing changes in the laboratory operations
2. Pattern of failure to document investigation of
discrepancies
3. Lack of validation of computerized and/or automated
processes
4. Pattern of inadequate sampling practices
5. Lack of validated analytical methods
6. Pattern of failure to follow approved analytical
procedures.
7. Pattern of failure to follow an adequate OOS procedure
8. Pattern of failure to retain raw data
9. Lack of stability indicating methods
10. Pattern of failure to follow stability programs
Significant deficiencies by system
FDAs_GMP_Inspection_with_special_regard_to_Aseptic_Process_for_Drugs___Biologicals_pf lee.ppt

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FDAs_GMP_Inspection_with_special_regard_to_Aseptic_Process_for_Drugs___Biologicals_pf lee.ppt

  • 1. FDA’s GMP Inspection with special regard to Aseptic Process for Drugs & Biologicals Professor Chung Keel Lee, Ph.D. Special Advisor to the Minister, MFDS Invited Professor, EWU & SNU Advisor to World Health Organization(WHO) Chair, Korea Affiliate, International Society for Pharmaceutical Engineering(ISPE) March 22, 2018 Gyeongin Regional Office of MFDS
  • 2. Thecountries visitedbyCKLasaninspector and/ortrainer since1987 2 Argentina Chile Denmark Korea Myanmar Taiwan Venezuela Australia China Indonesia Malaysia Philippines Thailand Vietnam Brazil Colombia Iran Mexico Russia USA Bulgaria Cuba Japan Mongolia Singapore Uzbekistan
  • 3. Contents • Four Basic Elements of CGMP : “4Ms” • System-based Inspection • Latest GMP Trends(QbD) • Sterile Drug Products Produced by Aseptic Processing • Significant Deficiencies by System-based Inspection • Question & Answer Session
  • 4. Four Basic Elements of CGMP “4Ms” Men Machinery Materials Methods Qualification Adequate training Products Reagents Components Containers & Closures Labels Manufacturing Control Validation Documentation Buildings Facilities Equipment Tools  “4Ms”
  • 5.  Men • Organization : Independence • Qualification • Training • Personnel Responsibilities Four Basic Elements of CGMP
  • 6.  Materials • Receipt • Sampling • Testing • Release • Retesting • Cell Banking • Viral Seeds • Reagents • Labels • Products Untested Components, Drug product Containers & Closures Four Basic Elements of CGMP
  • 7.  Machinery • Building Design • HVAC System • Water For Injection System • Clean Steam System • Washing & Toilet Facilities • Laminar Flow Hoods. HEPA filter Four Basic Elements of CGMP
  • 8. FDA Descriptive Class 100 Class 10,000 Class 100,000 ND In Operation ≥ 0.5㎛ /ft3 100 10,000 100,000 ND Action Level CFU/m3 1 10 100 ND EU, WHO, PIC/S Descriptive A B C D ND At Rest ≥ 0.5㎛ /m3 3,520 3,520 352,000 3,520,000 ≥ 5㎛ /m3 20 29 2,900 29,000 In Operation ≥ 0.5㎛ /m3 3,520 352,000 3,520,000 ND ≥ 5㎛ /m3 20 2,900 29,000 ND CFU/m3 < 1 < 10 < 100 < 200 ISPE Descriptive Grade 5 Grade 7 Grade 8 CNC+ CNC ISO Descriptive ISO. 5 ISO. 7 ISO. 8 ISO. 9 In Operation ≥ 0.5㎛ /m3 3,520 352,000 3,520,000 35,200,000 ≥ 5㎛ /m3 20 2,930 29,300 293,000 Comparison of Air Cleanliness Classifications
  • 9.  As-Built condition - Where the installation is complete with all services connected and functioning but with no equipment & personnel present.  At-Rest condition - Where the installation is complete with equipment installed and operating but with no personnel present.  Operational condition - Where the installation is functioning with the specified No. of personnel present & equipment operating. 3 Occupancy States
  • 10.  Methods • Production • Sampling & Testing • Environmental Monitoring • Packaging & Labeling • Validation • Documentation • Storage Drug Products Release Quality Control(QC) - Under appropriate conditions Quarantine - The oldest stock product is distributed first - A system to readily determine the distribution of drug Four Basic Elements of CGMP
  • 11.  Quality System  Facility & Equipment  Materials  Production  Laboratory Controls  Packaging & Labeling System Based Inspection
  • 12. CGMP Subpart Qual. F/E Mat. Prod PKG/L Lab. B. Organization & Personnel       C. Buildings & Facilities  D. Equipment  E. Control of Components & Drug Product containers & closures   F. Production & Process Controls   G. Packaging & Labeling Control   H. Holding & Distribution  I. Laboratory Controls   J. Records & Reports       K. Returned & Salvaged Drug Products   CGMP vs. Systems
  • 13.  Introduction  2002 : Pharmaceutical CGMP Initiative for the 21st Century-A Risk Based Approach The Pharmaceutical Quality for the 21st Century-A Risk Based Approach Latest GMP Trends(QbD)
  • 14. Research & Development Commercial Manufacturing Post-market Surveillance Pre-clinical Clinical Ⅰ Ⅱ Ⅲ Risk-based Approach Quality System Approach Traditional Enhanced The entire lifecycle of a product Latest GMP Trends(QbD)  Traditional vs. New Enhanced Approach
  • 15.  QTPP  CQA of the product  Input variables : materials etc.  Process parameters : temp., time, humidity etc.  Multidimensional combination & interaction → Design Space  Real time release (test)  Quality by Design → Regulatory flexibility Latest GMP Trends(QbD)  Ishikawa (Fishbone) Diagram (risk assessment tool)
  • 16.  US FDA’s Guidances with Enhanced Approach (QbD)  Sterile Drug Products Produced by Aseptic Processing –CGMP (Sept., 2004)  Process Analytical Technology (PAT) : A Framework for Innovative Pharmaceutical Development, Manufacturing & Quality Assurance (Sept., 2004)  Quality Systems Approach to Pharmaceutical CGMP Regulations (Sept., 2006)  Process Validation : General Principles & Practices (Jan., 2011) Latest GMP Trends
  • 17.  ICH Harmonized Tripartite Guidelines  Pharmaceutical Development (ICH Q8:R2) (Aug., 2009)  Quality Risk Management (ICH Q9) (Nov., 2005)  Pharmaceutical Quality System (ICH Q10) (June, 2008)  Development & Manufacture of Drug Substances (ICH Q11) (Nov., 2012) Latest GMP Trends
  • 18. Sterile Drug Products produced by Aseptic Processing I. Introduction II. Background III. Scope IV. Building & Facilities V. Personnel Training VI. Components & Containers/Closures VII. Endotoxin Control VIII. Time Limitations IX. Validation of Aseptic Processing & Sterilization X. Laboratory Controls XI. Sterility Testing XII. Batch Record Review
  • 19. I. Introduction • Replacement of 1987 guideline on sterile drug products produced by aseptic processing (aseptic processing guideline) • When manufacturing sterile drug and biological products using aseptic processing
  • 20. II . Background A. Regulatory Framework  Where it is impossible to comply with the applicable regulations in both parts 600 through 680 and parts 210 & 211, the regulation specifically applicable to the drug product in question shall supercede the more general regulations.
  • 21. III. Scope • This guidance updates the 1987 Aseptic Processing Guideline with respect to: – personnel qualification – cleanroom design – process design – quality control – environmental monitoring – review of production records
  • 22. IV. Buildings and Facilities • Clean area air classifications: measured at work level under dynamic conditions * You may establish alternate levels due to the nature of the operation or method of analysis. ** Normally yield no microbiological contaminants. Clean Area Classification (≥ 0.5 mm particles/ft3) ISO Designation > 0.5 mm particles/m3 *CFU/m3 (active S.) *CFU/4-hr (passive S. diam. 90mm) 100 5 3,520 <1** <1 1000 6 35,200 <7 <3 10,000 7 352,000 <10 <5 100,000 8 3,520,000 <100 <50
  • 23. IV. Buildings and Facilities A. Critical Area-Class 100 (ISO 5)  A critical area is one in which the sterilized drug product, containers, and closures are exposed to environmental conditions that must be designed to maintain product sterility.  Particles: – Extraneous contaminant themselves – Act as a vehicle for microorganisms. – To be measured not more than 1 foot away from the work site. – Regular monitoring should be performed during each production shift.
  • 24. IV. Buildings and Facilities A. Critical Area-Class 100 (ISO 5)  High levels of product particles – Qualification of the area under dynamic conditions without actual filling function  In situ air pattern under dynamic conditions – Unidirectional air flow – Sweeping action over & away from the product • A velocity of 0.45 meters/second (90 feet/minute) ±20%
  • 25. IV. Buildings and Facilities B. Supporting Clean Areas  To be designed to minimize the level of particle contaminants & microbiological content (bioburden)  The area immediately adjacent to the aseptic processing line should meet, at a minimum, class 10,000 (ISO 7) standards under dynamic conditions. Class 1,000 (ISO 6) or Class 100 may apply to this area.  Class 100,000 (ISO 8) air cleanliness level is appropriate for less critical activities (e.g., equipment cleaning).
  • 26. IV. Buildings and Facilities C. Clean Area Separation  Airflow from higher cleanliness area to adjacent less clean areas.  A substantial positive pressure differentials for rooms of higher air cleanliness  10-15 Pa (0.04-0.06 inches of water gauge ) maintained between rooms of differing classification with doors closed.
  • 27. IV. Buildings and Facilities C. Clean Area Separation  At least 12.5 Pa should be maintained between the aseptic processing room and unclassified room adjacent to the aseptic processing room.  Pressure differentials should be monitored continuously & frequently recorded.
  • 28. IV. Buildings and Facilities C. Clean Area Separation • For class 100,000 (ISO 8) at least 20 air changes per hour is acceptable. Significantly higher air change rates are normally needed for class 10,000 & Class 100 areas. • A suitable facility monitoring system (i.e., alarms) is needed.
  • 29. IV. Buildings and Facilities D. Air Filtration 1. Membrane  Membrane filters (sterile) can be used for compressed gas, autoclave air lines, lyophilizer vacuum breaks, tanks containing sterilized materials.  Gas filters (including vent filters) should be dry.  Filters that supply sterile gases should be integrity tested upon installation & periodically thereafter (e.g., end of use).
  • 30. IV. Buildings and Facilities D. Air Filtration 2. HEPA • Leak testing at installation • 2 x / year for aseptic processing room • Facility renovation, media fill failure, drug product sterility failure... : additional testing • Leak test on dry heat depyrogenation tunnels & ovens(e.g. glass vials)
  • 31. IV. Buildings and Facilities D. Air Filtration 2. HEPA • DOP (DiOctylPhthalate) or PAO (Poly-Alpha-Olefin) – Leak testing aerosols • Alternative aerosols – Not promoting microbial growth • Filter efficiency test – Monodispersed aerosol of 0.3μ particles – Retaining at least 99.97%
  • 32. IV. Buildings and Facilities D. Air Filtration 2. HEPA  Filter Integrity test – Polydispersed aerosol (mean < 1μ but > 0.3 μ) – Sufficient No. of particles at ~0.3μ. – Test in place – Scan at 1~2 inches from the filter face – Sampling rate at ≥1 ft3/min. – > 99.99% retention or < 0.01% leak • Uniformity of velocity across the filter – Variations in velocity can cause turbulence. – Velocity of unidirectional air » At 6 inches from the filter face and » At work level in critical area
  • 33. IV. Buildings and Facilities E. Design • Aseptic processes designed to minimize exposure of sterile articles to contamination hazards • Flow of personnel, materials, products, equipment, air & waste • Minimum No. of personnel in aseptic processing area • SIP (sterilize-in-place) or automation of processes can reduce risk to the product.
  • 34. IV. Buildings and Facilities E. Design • A partially closed sterile product should be transferred only in critical areas. – The area between a filling line & the lyophilizer • Appropriately designed transfer equipment can be qualified for this purpose. • Airlocks with interlocking doors between aseptic processing area entrance and unclassified area. • Stoppered vials should be under protection until completion of the crimping step.
  • 35. IV. Buildings and Facilities E. Design • Seamless & rounded floor to wall junctions, readily accessible corners… • Sanitary fittings & valves for processing equipment • No drains in aseptic processing areas • Avoid horizonal surfaces or ledges • SOPs on returning a facility to operating conditions following a shutdown
  • 36. V. Personnel Training A. Personnel • Evaluate each operator’s conformance to written procedures during operation. • QC’s regular oversight on adherence to established, written procedures during manufacturing • Techniques to maintain sterility of sterile items & surfaces: – Contact sterile materials only with sterile instruments. – Move slowly and deliberately.
  • 37. V. Personnel Training A. Personnel • Techniques to maintain sterility of sterile items & surfaces: – Keep the entire body out of the path of unidirectional airflow. – Approach from the side & not above the production in vertical laminar flow. – Refrain from speaking when in direct proximity to the critical area. – Maintain proper gown control.
  • 38. V. Personnel Training A. Personnel  Gowns: sterile, nonshedding, covering the skin & hair – Common elements of gowns: face-masks, hoods, beard/moustache covers, protective goggles – Adequate barrier should be created by the overlapping of gown components. – Gloves should be sanitized frequently. • Microbiological surface sampling of several locations on gown : e.g., glove fingers, facemask, forearms, chest etc.
  • 39. V. Personnel Training A. Personnel • Periodic requalification following an initial assessment of gowning • Annual requalification for automated operations B. Laboratory Personnel • The basic principles of training, aseptic technique, and personnel qualification in aseptic manufacturing also are applicable to those performing aseptic sampling and microbiological laboratory analyses.
  • 40. V. Personnel Training C. Monitoring Program  Obtain surface samples of each operator's gown including gloves & other locations of the gown on a daily basis, or in association with each lot.  Asepsis is fundamental to an aseptic processing operation.  Sanitizing gloves just prior to sampling is inappropriate because it can prevent recovery of microorganisms that were present during an aseptic manipulation.
  • 41. VI. Components and Container/Closures A. Components  Active ingredients, water for injection (WFI), and other excipients: acceptable limits of microbial content (e.g., bioburden, endotoxin) should be established.  Sterile-filtration of a solution formed by dissolving the component (s) in a solvent such as WFI, USP, is used when the solution is adversely affected by heat.
  • 42. VI. Components and Container/Closures A. Components  Dry heat sterilization is good for components that are heat stable and insoluble. Heat penetration & distribution studies are needed for powder sterilization because of the insulating effects of the powder.  Irradiation can be used to sterilize some components.
  • 43. VI. Components and Container/Closures B. Containers/Closures 1. Preparation • Containers & closures should be sterile and, for parenteral drug nonpyrogenic. • Time limits for holding sterile & depyrogenated containers & closures • Final rinse water should be purified water and, for parenteral products WFI, USP. • Subjecting glass containers to dry heat accomplishes both sterilization & depyrogenation.
  • 44. VI. Components and Container/Closures B. Containers/Closures 1. Preparation • Ethylene oxide (EtO) : effective surface sterilant – Temperature, pressure, humidity, gas concentration, exposure time, degassing, aeration, & residuals should be specified & monitored. – Biological indicators are of special importance in demonstrating the effectiveness of EtO & other gas sterilization processes. • Rubber closures (e.g., stoppers and syringe plungers) : – Multiple cycles of washing / rinsing prior to sterilization
  • 45. VI. Components and Container/Closures B. Containers/Closures 1. Preparation • Rubber closures (e.g., stoppers and syringe plungers) : – Initial rinses with PW, USP followed by – Final rinse with WFI, USP for parenteral products – Depyrogenation by multiple rinses of hot WFI – The time between washing / drying and sterilizing should be minimized. – Siliconization of rubber stoppers: potential sources of contamination • Visual identification & Certificate of Analysis review on containers & closures may be accepted with the reliability of the supplier’s test results established at appropriate intervals.
  • 46. VII. Endotoxin Control • Endotoxin contamination of an injectable product can occur as a result of poor CGMP controls. • Drug product components, containers, closures, storage time limitations, and manufacturing equipment are among the areas to address in establishing endotoxin control. • Adequate cleaning, drying, and storage of equipment will control bioburden and prevent contribution of endotoxin load.
  • 47. VII. Endotoxin Control • Sterilizing-grade filters and moist heat sterilization have not been shown to be effective in removing endotoxin. • Some clean-in-place procedures employ initial rinses with appropriate high purity water and/or a cleaning agent (e.g., acid, base, surfactant), followed by final rinses with heated WFI. • Equipment should be dried following cleaning, unless the equipment proceeds immediately to the sterilization step.
  • 48. VIII. Time Limitations • Time limits for each phase of aseptic processing – Between the start of bulk product compounding and its sterilization filtration – Product exposure while on the processing line – Storage of sterilized equipment, containers & closures • Bioburden & endotoxin load should be assessed to establish time limits for stages. • The total time for product filtration should be limited to an established maximum: – To prevent microorganisms from penetrating the filter – To prevent an increase in upstream bioburden & endotoxin load
  • 49. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations  An aseptic processing operation should be validated using a microbiological growth medium in place of the product. This ”process simulation” (media fill) includes exposing the microbiological growth medium to product contact surfaces of equipment, container closure systems, critical environments, and process manipulations to closely simulate the same exposure that the product itself will undergo during actual operations (e.g., start-up, sterile ingredient additions, aseptic connections, filling, closing).
  • 50. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations • Aseptic processing validation: – Microbial growth medium – Process simulation (media fill) – Exposure to product contact surfaces – The sealed containers filled with the medium are incubated. – Results are interpreted to assess the potential for a unit of drug product to become contaminated during actual operations. – Environmental monitoring data from the process simulation can also provide useful information for the processing line evaluation
  • 51. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 1. Study Design for Media Fill a. Consider the following issues: simulate actual operations + worst-case conditions  Factors associated with the longest permitted run: e.g., operator fatigue  normal interventions & nonroutine interventions (stoppages, equipment adjustments)
  • 52. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 1. Study Design for Media Fill a. Consider the following issues: simulate actual operations + worst-case conditions  Lyophilization, when applicable  Aseptic assembly of equipment (e.g., at start-up, during processing)  Number of personnel and their activities  Representative number of aseptic additions or transfers  Shift changes, breaks, and gown changes (when applicable)  Type of aseptic equipment disconnections/connections
  • 53. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 1. Study Design for Media Fill a. Consider the following issues: simulate actual operations + worst-case conditions  Aseptic sample collections  Line speed & configuration  Weight checks  Container closure systems (e.g., sizes, type) b. A written batch record should be prepared for each media fill run.
  • 54. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 2. Frequency and Number of Runs  At least 3 consecutive separate successful runs should be performed during initial line qualification.  Subsequently, routine semi-annual qualification conducted for each processing line will evaluate the state of control of the aseptic process.  All personnel authorized to enter the aseptic processing room during manufacturing (i.e., technicians, maintenance personnel…) should participate in a media fill at least once a year.  Facility & equipment modifications, line configuration changes, significant changes in personnel, anomalies in environmental testing results, container closure system changes, extended shutdowns, or end product sterility testing showing contaminated products may be cause for revalidation of the system.
  • 55. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 3. Duration of runs  When aseptic processing employs manual filling or closing, or extensive manual manipulations, the duration of the process simulation should be no less than the length of the actual manufacturing process to best simulate contamination risks posed by operators.  For lyophilization operations FDA recommends that unsealed containers be exposed to partial evacuation of the chamber but the vials should not be frozen & the medium should remain in an aerobic state.
  • 56. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 4. Size of runs • 5,000 to 10,000 units • Maximum batch size if the run size is under 5,000 • Full or close to full batch size for manually intensive filling • Lower number of units in case of using an isolator due to the lack of direct human intervention.
  • 57. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 5. Line Speed  Each media fill run should evaluate a single line speed, and the speed chosen should be justified. 6. Environmental Condition  Media fills should be adequately representative of the conditions under which actual manufacturing operations are conducted.
  • 58. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 7. Media • “soybean casein digest medium” in general • Growth promotion test : e.g., USP indicator organisms – Gram-positive & gram-negative bacteria – Yeast – Mold • Substituted challenge : isolates from E.M. & sterility test • <100 CFU challenge/unit  Each unit should be filled with an appropriate quantity of microbial growth medium to contact the inner container/ closure surfaces (the unit is inverted or swirled).
  • 59. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 8. Incubation & Examination of Media-Filled Units • 20-30 ℃ ± 2.5℃ • Not less than 14 days • If two temperatures are used: – ≥ 7 days at 20-25 ℃, first – ≥ 7 days at 30-35 ℃, second • QC unit’s involvement – Observation or – Oversight throughout the examination • All suspect units should be brought to QC microbiologist.
  • 60. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 8. Incubation & Examination of Media-Filled Units • Clear containers for amber or opaque containers • All integral units → incubation • Units not related to integrity (cosmetic defect) → incubation • Units that lack integrity should be rejected. • Criteria for yield ( total units incubated / total units filled)
  • 61. IX. Validation of Aseptic Processing and Sterilization A. Process Simulations 9. Interpretation of Test Results  The process simulation run should be observed by the QC Unit.  Contaminated units should be reconcilable with the approximate time and the activity being simulated during the media fill.  Any contaminated unit should be identified to species level.  Any failure investigation should assess the impact on commercial drugs produced on the line since the last media fill.  Modern aseptic processing operations should normally yield no media fill contamination.
  • 62. IX. Validation of Aseptic Processing and Sterilization B. Filtration Efficacy • 0.22μ or 0.2 μ sterilization grade filters • Sterile filtration validation: – Microbial challenges – Integrity test of the filters • Brevundimonas diminuta (ATCC 19146) • At least 107 organisms per cm2 of effective filter area • No passage of the challenge microorganisms
  • 63. IX. Validation of Aseptic Processing and Sterilization B. Filtration Efficacy • Minimize the bioburden of the unfiltered product. • Direct inoculation into the drug formulation is preferred. • Worst-case conditions : maximum filter use time & pressure • Filter integrity testing : before & after use • Forward flow and bubble point tests
  • 64. IX. Validation of Aseptic Processing and Sterilization C. Sterilization of Equipment, Containers, and Closures • Moist heat and dry heat sterilization 1. Qualification & Validation • Requalification on a periodic basis • Remove air from the autoclave chamber. • Filter installations in piping (SIP) – Pressure differential across the filter – Significant temperature drop on the downstream – Place biological indicators at downstream locations of the filter.
  • 65. IX. Validation of Aseptic Processing and Sterilization C. Sterilization of Equipment, Containers, and Closures • Moist heat and dry heat sterilization 1. Qualification and Validation • Empty chamber studies : – Temperature & pressure mapping study with calibrated measurement devices – Heat penetration studies on loading configurations – In general, the biological indicator should be placed adjacent to the temperature sensor to assess the correlation between microbial lethality and predicted lethality based on thermal input.
  • 66. IX. Validation of Aseptic Processing and Sterilization C. Sterilization of Equipment, Containers, and Closures • Moist heat and dry heat sterilization 1. Qualification and Validation  Articles difficult to sterilize: filters, filling manifolds, pumps. Some other examples include certain locations of tightly wrapped or densely packed supplies, securely fastened load articles, lengthy tubing, the sterile filter apparatus, hydrophobic filters, and stopper load.  A sterility assurance level of 10-6 or better should be demonstrated for a sterilization process.
  • 67. IX. Validation of Aseptic Processing and Sterilization C. Sterilization of Equipment, Containers, and Closures • Moist heat and dry heat sterilization 1. Qualification and Validation  For more information, refer to “ Guideline for the Submission of Documentation for Sterilization Process Validation in Applications for Human and Veterinary Drug Products”.  Change control procedures should adequately address issues such as a load configuration change or a modification of a sterilizer.
  • 68. IX. Validation of Aseptic Processing and Sterilization C. Sterilization of Equipment, Containers, and Closures • Moist heat and dry heat sterilization 2. Equipment Controls & Instrument Calibration • For both validation & routine process control, calibrate: – Temperature & pressure monitoring devices – Sensing devices before and after validation runs – Devices used to monitor dwell time in the sterilizer – D-value (resistance) of a biological indicator (e.g., spore strips, glass ampuls) can be accepted if the reliability of a vendor’s COA is established. – The microbial count of a B.I.
  • 69. IX. Validation of Aseptic Processing and Sterilization C. Sterilization of Equipment, Containers, and Closures • Moist heat and dry heat sterilization 2. Equipment Controls & Instrument Calibration  For both validation & routine process control, calibrate : - For dry heat depyrogenation tunnels, devices used to measure belt speed should be routinely calibrated. - Routine evaluation of sterilizer performance- indicating attributes, such as equilibrium (come up) time is important in assuring that the unit continues to operate as per the validated conditions.
  • 70. X. Laboratory Controls A. Environmental Monitoring 1. General Written Program  In aseptic processing, one of the most important laboratory controls is the environmental monitoring program.  Monitoring should cover all production shifts.  Evaluate the quality of air & surfaces: – Air, floors, walls, equipment surfaces (especially critical surfaces) – Critical surfaces : come in contact with the sterile product, containers, & closures.
  • 71. X. Laboratory Controls A. Environmental Monitoring 1. General Written Program  Written procedures (SOPs) should include : – Locations to be sampled – Sample timing ; i.e., during or at the conclusion of operations – Sample frequency – Duration of sampling – Sample size : e.g., surface area, air volume – Sampling equipment & techniques – Alert & action levels – Appropriate response to deviations from alert or action levels
  • 72. X. Laboratory Controls A. Environmental Monitoring 1. General Written Program  Samples should be taken throughout the classified areas of the aseptic processing facility (e.g., aseptic corridors, gowning rooms).  Sample sizes should be sufficient to optimize detection of environmental contaminations at levels that might be expected.  Critical surface sampling should be performed at the conclusion of the aseptic processing operation to avoid direct contact with sterile surfaces during processing.
  • 73. X. Laboratory Controls A. Environmental Monitoring 2. Establishing Levels & a Trending Program  Alert & action levels – Based on the relationship of the sampled location to the operation – Based on the need to maintain adequate control – Consider E.M.data from historical databases, media fills, clean room qualification & sanitization studies.  QC unit should provide routine oversight of trends in environmental & personnel monitoring data. – Near-term trends: daily, weekly, monthly & quarterly – Long-term trends: yearly, biennially,….
  • 74. X. Laboratory Controls A. Environmental Monitoring 3. Disinfection Efficacy  Disinfectants should be sterile, in suitable containers (e.g., sterile) and used for no longer than the predefined period .  Routinely used disinfectants should be effective against the normal microbial vegetative flora recovered from the facility.  Many common disinfectants are ineffective against spores.  Disinfection procedures should be described in detail e.g., preparation, work sequence, contact time etc.
  • 75. Definitions  Sanitization : Reduces viable microorganisms to a defined acceptable level. Normally achieved by using a chemical agent or heat.  Disinfection : Process by which viable microbiological agents or eukaryotic cells are reduced to a level unlikely to produce disease in healthy people, plants or animals.  Decontamination : A process that reduces contaminating substances to a defined acceptable level  Pasteurization : The heating of milk, wines, fruit juices, etc. for about 30 min. at 62-68℃ whereby the living bacteria are destroyed, but the flavor or bouquet is preserved.  Sterilization : Destroys or eliminates all viable microbes including bacterial spores.
  • 76. Definitions (continued)  Antiseptic : Acting against sepsis. An antiseptic agent is one that has been formulated for use on living tissue(mucous membrane or skin) to prevent or inhibit growth or action of organisms.  Pyrogen : A fever-producing substance called also pyretogen, pyretic, pyrectic Bacterial pyrogen : a fever producing agent of bacterial origin : endotoxin  Endotoxin : Lipopolysaccharide Integral part of the bacterial (gram negative) cell wall & is only released when the integrity of the wall is disturbed.  Depyrogenation : The removal or destruction of pyrogen (endotoxins)
  • 77. X. Laboratory Controls A. Environmental Monitoring 4. Monitoring Methods for Biological Quality a. Surface monitoring  Product contact surfaces, floors, walls & equipment  Touch plates, swabs & contact plates b. Active air monitoring  Active devices : impaction, centrifugal and membrane (or gelatin) samplers  Quantitative air monitoring c. Passive air monitoring (settling plates)  Settling plates: Petri dishes containing nutrient growth medium exposed to the environment  Qualitative, or semi-quantitative air monitoring.  Exposure conditions should preclude desiccation (e.g., caused by lengthy sampling periods and/or high airflows), which inhibits recovery of microorganisms.
  • 78. A. Environmental Monitoring 5. Recommended action level of microbiological quality (Air) Clean Area Classification (0.5mm particles/ft3) ISO Designation 0.5mm particles/m3 Microbiological Active Air Action Levels (CFU/m3) Microbiological Settling Plates Action Levels (diam. 90mm:cfu/4 hrs.) 100 5 3,520 1 1 1,000 6 35,200 7 3 10.000 7 352,000 10 5 100,000 8 3,520,000 100 50 US FDA, 2004 : Sterile Drug Products Produced by Aseptic Processing-CGMP X. Laboratory Controls
  • 79. A. Environmental Monitoring 6. Recommended action level of microbiological quality (Surface) Clean Area Classification (0.5mm particles/ft3) ISO Designation 0.5mm particles/m3 Equipment Gloves Clothing CFU / Contact Plate (24-30 cm2) CFU / Contact Plate (24-30 cm2) CFU / Contact Plate (24-30 cm2) 100 5 3,520 3 (including floor) 3 5 1,000 6 35,200 – – – 10.000 7 352,000 5 10 (floor) 10 20 100,000 8 3,520,000 – – – USP <1116>, 2006 : Microbiological Evaluation of Clean Rooms & Other Controlled Environment X. Laboratory Controls
  • 80. X. Laboratory Controls B. Microbiological Media & Identification • Routine identification of microorganisms to the species levels • Culture media capable of detecting fungi (i.e., yeasts and molds) & bacteria • Total aerobic bacterial count at 30~35℃ for 48~72 hours • Total combined yeast & mold count at 20~25℃ for 5~7 days • Growth promotion testing on all lots of prepared media
  • 81. X. Laboratory Controls C. Prefiltration Bioburden • Bioburden can contribute impurities (e.g., endotoxin) to, & lead to degradation of, the drug product. • Minimize the bioburden in the unfiltered product. • A prefiltration bioburden limit should be established. D. Alternate Microbiological Test Methods : • Rapid test methods : equivalent or better E. Particle monitoring • Routine particle monitoring is useful in rapidly detecting deviations in air cleanliness. • A result outside the established classification level at a given location should be investigated.  The investigation should include an evaluation of trending data.
  • 82. XI. Sterility Testing • Sterility testing lab. environment : comparable to aseptic filling operations • Use of isolator for sterility testing minimizes false positive test result. A. Microbiological Laboratory Controls • Method validation : microbiological challenge • If growth is inhibited : – Increased dilution – Additional membrane filter washes – Addition of inactivating agents • Media : sterile & growth promoting • Personnel qualification & training
  • 83. XI. Sterility Testing B. Sampling & Incubation • Limited ability to detect contamination due to small sample size (USP): – 10,000-unit lot with 0.1 % contamination : 20 unit sample test would pass the lot with 98% chance. – If 10% of the lot are contaminated, contamination can be detected about 9 out of 10 cases.
  • 84. XI. Sterility Testing B. Sampling & Incubation  The samples should represent the entire and processing conditions. Samples should be taken: – At the beginning, middle, and end of the aseptic processing operation – In conjunction with processing interventions or excursions  Because of the limited sensitivity of the test, any positive result is considered a serious CGMP issue that should be thoroughly investigated.
  • 85. XI. Sterility Testing C. Investigation of Sterility Positives • A positive test would be invalid only when microbial growth can be unequivocally ascribed to laboratory error. When available evidence is inconclusive, batches should be rejected. • Investigation's persuasive evidence of the origin of the contamination should be based on : 1. Identification (speciation) of the organism in the sterility test  To the species level  Determine to see the organism in lab. & production environment  Advanced identification method (e.g., nucleic-acid based) are valuable for investigation.  When comparing the results from E.M. and sterility positives the same methodology should be used for identifications.
  • 86. XI. Sterility Testing C. Investigation of Sterility Positives  The investigation's persuasive evidence of the origin of the contamination should be based on: 2. Record of Laboratory Tests & Deviation 3. Monitoring of Production area Environment :  Trend analysis of microorganisms in the critical and immediately adjacent areas  Look at both short - and long - term environmental trend analyses. 4. Monitoring Personnel • Review of data & associated trends from daily monitoring of personnel. • Adequacy of personnel practices & training
  • 87. XI. Sterility Testing C. Investigation of Sterility Positives  The investigation's persuasive evidence of the origin of the contamination should be based on : 5. Product Presterilization Bioburden 6. Production Record Review  Events that could have impacted on the critical zone  The functioning of utility and/or support systems  Whether construction or maintenance activities could have had an adverse impact 7. Manufacturing History  Past deviations, problems, or changes on process, components, equipment etc.
  • 88. XII. Batch Record Review: Process Control Documentation • All in-process & laboratory control results must be included in the batch production record. • Essential elements of the batch release decision: – Review of environmental & personnel monitoring data – Review the data relating support systems (HEPA, HVAC, WFI, steam generator) – Review the data on proper functioning of equipment (e.g., batch alarms report, integrity of various filters)
  • 89. XII. Batch Record Review: Process Control Documentation • Interventions and/or stoppages (unplanned) should be documented in batch records with the associated time & duration of the event. • Any disruption in power supply that could affect product quality must be included in batch production records.
  • 90. Significant Deficiencies by System A. Quality System B. Facilities and Equipment System C. Materials System D. Production System E. Packaging and Labeling System F. Laboratory Controls System
  • 91. A. Quality System 1. Pattern of failure to review/approve procedures 2. Pattern of failure to document execution of operations as required 3. Pattern of failure to review documentation 4. Pattern of failure to conduct investigations and resolve discrepancies/failures/deviations/complaints 5. Pattern of failure to assess other systems to assure compliance with GMP and SOPs Significant deficiencies by system
  • 92. B. Facilities and Equipment 1. Contamination with filth, objectionable microorganisms, toxic chemicals or other drug chemicals, or a reasonable potential for contamination, with demonstrated avenues of contamination, such as airborne or through unclean equipment 2. Pattern of failure to validate cleaning procedures for non-dedicated equipment. Lack of demonstration of effectiveness of cleaning for dedicated equipment 3. Pattern of failure to document investigation of discrepancies 4. Pattern of failure to establish/follow a control system for implementing changes in the equipment 5. Pattern of failure to qualify equipment, including computers Significant deficiencies by system
  • 93. C. Materials System 1. Release of materials for use or distribution that do not conform to established specifications 2. Pattern of failure to conduct one specific identity test for components 3. Pattern of failure to document investigation of discrepancies 4. Pattern of failure to establish/follow a control system for implementing changes in the materials handling operations 5. Lack of validation of water systems as required depending upon the intended use of the water 6. Lack of validation of computerized processes Significant deficiencies by system
  • 94. D. Production System 1. Pattern of failure to establish/follow a control system for implementing changes in the production system operations 2. Pattern of failure to document investigation of discrepancies 3. Lack of process validation 4. Lack of validation of computerized processes 5. Pattern of incomplete or missing batch production records 6. Pattern of nonconformance to established in-process controls, tests, and/or specifications Significant deficiencies by system
  • 95. E. Packaging and Labeling System 1. Pattern of failure to establish/follow a control system for implementing changes in the packaging and/or labeling operations 2. Pattern of failure to document investigation of discrepancies 3. Lack of validation of computerized processes 4. Lack of control of packaging and labeling operations that may introduce a potential for mislabeling 5. Lack of packaging validation. Significant deficiencies by system
  • 96. F. Laboratory Controls System 1. Pattern of failure to establish/follow a control system for implementing changes in the laboratory operations 2. Pattern of failure to document investigation of discrepancies 3. Lack of validation of computerized and/or automated processes 4. Pattern of inadequate sampling practices 5. Lack of validated analytical methods 6. Pattern of failure to follow approved analytical procedures. 7. Pattern of failure to follow an adequate OOS procedure 8. Pattern of failure to retain raw data 9. Lack of stability indicating methods 10. Pattern of failure to follow stability programs Significant deficiencies by system