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Manufacture of sterile medicines –
1
Sterilization - validation,
qualification requirements
Mrs Robyn Isaacson
Manufacture of sterile medicines –
2
Sterilization - Overview
Objectives
– Discuss definition of “Sterile”
– Briefly describe sterilization methods
– Describe approaches to be used for the
validation of a sterilization process using
Moist Heat as an example
– Describe requirements for routine monitoring
and control of sterilization
– Review issues that are specific to other
sterilization processes
Manufacture of sterile medicines –
3
Sterile Products - Overview
• Certain pharmaceutical products must be sterile
– injections, ophthalmic preparations, irrigations solutions,
haemodialysis solutions
• Two categories of sterile products
– those that can be sterilised in final container (terminally
sterilised)
– those that cannot be terminally sterilised and must be
aseptically prepared
Manufacture of sterile medicines –
4
Sterilization - Overview
What is the definition of “sterile”?
• Free from microorganisms
In practice no such absolute statement regarding absence
of microorganisms can be proven
• Defined as the probability of 1 in a million of a
container being contaminated (10-6
)
• This referred to as the Sterility Assurance Level
(SAL)
• Organisms are killed in an exponential fashion
Manufacture of sterile medicines –
5
Definition of “Sterile”
MICROBIAL INACTIVATION
Nt = Noe
-kt
0
200
400
600
800
1000
1200
Time
Noofsurvivingorganisms
-2.00
-1.50
-1.00
-0.50
0.00
0.50
1.00
1.50
2.00
2.50
3.00
3.50
No remaining
Log No remaining
No remaining 1000 368 135 50 18 7 2 1 0 0 0
Log No remaining 3.00 2.57 2.13 1.70 1.26 0.83 0.39 -0.04 -0.47 -0.91 -1.34
0 1 2 3 4 5 6 7 8 9 10
Manufacture of sterile medicines –
6
Definition of “Sterile”
Microbial Inactivation
-3
-2
-1
0
1
2
3
4
1 2 3 4 5 6
Time
LogNoofSurvivingOrganisms
D-value - Time (or dose) required to reduce the
population of organisms by 1 log (or 90%)
D-Value
Resistance of an organism is referred as its “D-value”
Manufacture of sterile medicines –
7
Definition of “Sterile”
• A sterilization process must deliver a
Sterility Assurance Level (SAL) of 1 in a
million (10-6
)
• It is not possible to measure “10-6
”
• The required SAL can be achieved by
applying a process that will reduce the
number of organisms to zero and then
apply a safety factor that will deliver an
extra 6 log reduction
Manufacture of sterile medicines –
8
Definition of “Sterile”
Example
• For an initial bioburden of 102
the
sterilization process will need to
achieve an 8 log reduction in
viable organisms
• This will require 8 times the D-
value (e.g. if the organism has a
D value of 2 minutes then 8 x 2 =
16 minutes will be required to
achieve an 8 log reduction and
an SAL of 10-6
) (Point Z)
Microbial Death Curve
-7
-6
-5
-4
-3
-2
-1
0
1
2
0 1 2 3 4 5 6 7 8
Time
LogNoofSurvivors
Y
Z
Manufacture of sterile medicines –
9
Sterilization - Overview
Commonly used methods of sterilization
– Moist Heat
– Dry Heat
– Gas (Ethylene oxide)
– Radiation (Gamma or Electron)
– Filtration
– Others - UV, Steam and formaldehyde,
hydrogen peroxide
Manufacture of sterile medicines –
10
Moist Heat
• Saturated steam
• Common cycles:
– 121°C for 15 minutes
– 134°C for 3 minutes
– Other cycles of lower temperature and longer
time may be used (e.g. 115°C for 30 minutes)
• Used for sterilization of:
– terminal sterilization of aqueous injections,
ophthalmic preparations, irrigation &
haemodialysis solutions, equipment used in
aseptic processing
Manufacture of sterile medicines –
11
Moist Heat
• not suitable for non-aqueous/dry
preparations
• preferred method of sterilization
Manufacture of sterile medicines –
12
Dry Heat
• Lethality due to oxidative processes
• Higher temperatures and longer exposure
times required
• Typical cycles:
– 160°C for 120 minutes
– 170°C for 60 minutes
– 180°C for 30 minutes
– tunnels used for the sterilisation of glass vials
may use much higher temperatures (300°) for a
much shorter period
Manufacture of sterile medicines –
13
Dry Heat
• Used for:
– glassware and product containers used in
aseptic manufacture, non aqueous
thermostable powders and liquids (oils)
• also used for depyrogenation of glassware
(≥250°C)
– (Pyrogens - substances found in cell wall of
some bacteria which can cause fever when
introduced into the body)
Manufacture of sterile medicines –
14
Ethylene Oxide Gas
• Either pure or in mixtures with other inert
gases
• Requires presence of moisture
• Complex process
• Typical cycles:
– 1-24hours
– 25-1200 mg/L gas
– 25-65°C
– 30-85% relative humidity
Manufacture of sterile medicines –
15
Ethylene Oxide
• Used for:
– heat labile product containers
– surface sterilization of powders
• Adequate aeration to reduce toxic
residues
Manufacture of sterile medicines –
16
Radiation
• Gamma rays generated by Cobalt 60 or Caesium
137 radionuclides; or
• Accelerated electrons from an electron generator
• 25 kilograys (kGy) usual dose
– dose dependent on bioburden (resistance of organisms
not predictable)
• process must be properly validated
• used for:
– dry pharmaceutical products
– heat labile product containers
• can cause unacceptable changes
Manufacture of sterile medicines –
17
Filtration
• Removes organisms from liquids and
gasses
• 0.2 - 0.22 micron for sterilization
• composed of cellulose esters or other
polymeric materials
• filter material must be compatible with
liquid being filtered
• used for bulk liquids, gasses and vent
filters
Manufacture of sterile medicines –
18
Validation - Overview
• Selection of sterilzation process must be
appropriate for product
– terminal sterilization is the method of choice
– moist heat (autoclaving) is the most common
process used for terminal sterilization
– product must not be affected by heat
– container/closure integrity must be established
– items being sterilised must contain water (if
sealed) or material must allow for removal of
air and penetration of steam for steam (moist
heat) sterilization
Manufacture of sterile medicines –
19
Validation - Protocol
Requirements for Moist Heat Sterilization
Other processes follow similar requirements
• Validation protocol should include the
following details for each sterilization
process
– process objectives in terms of product type,
container/closure system, SAL required
– specifications for time, temperature, pressure
and loading pattern
– description of all equipment and support
systems in terms of type, model, capacity and
operating range
Manufacture of sterile medicines –
20
Validation - Protocol
Moist Heat continued:
– performance characteristics of all equipment
e.g. pressure gauges, valves, alarm systems,
timers, steam flow rates/pressures, cooling
water flow rates, cycle controller functions,
door closure gasketing and air break systems
and filters
– methodology for monitoring performance of
equipment and the process and labatory
testing methodology
– personnel responsible for all stages and final
evaluation (should have experience and
necessary training and be authorized)
Manufacture of sterile medicines –
21
Validation - Calibration
• Laboratory testing should be performed
by a competent laboratory, methodology
should be documented
• All instruments must be calibrated e.g.
– temperature recorders and sensors
– thermocouples
– pressure sensors for jacket and chamber
– timers
– conductivity monitors for cooling water
– flow metres for water/steam
– water level indicators when cooling water is used
– thermometers including those for thermocouple
reference, chamber monitoring and laboratory testing
Manufacture of sterile medicines –
22
Validation - Calibration
• Indicators should be calibrated
– physical and chemcial indicators should be tested
to demonstrate acceptable response to time and
temperature
– biological indicators should be tested for count
and time/temperature exposure response
• for commercial indicators - test certificate with count
and D-value and exposure response should be
available. Results acceptable if verified “in house”
periodically.
• In house indicators must be fully characterized (D-
value, identification) and appropriate for sterilization
process
All indicators should be appropriately stored and
within expiry
Manufacture of sterile medicines –
23
Validation - Cycle Development
• Concept of Fo
– Lethality factor equivalent to time at 121°C
• 1 minute at 121°C is equivalent to Fo of 1.
• Lethality can accumulate during heat up and cool
down phases
Typical temperature profile of a heat sterilization process
What would be the Fo of a cycle at 121°C for 15 minutes?
Manufacture of sterile medicines –
24
Validation - Cycle Development
• Fo is calculated using the following
equation:
Fo = ΔtΣ10(T-121/Z)
where:
• “Δt” is the time interval between measurements of
temperature (T)
• “T” is the temperature of sterilised product at time (t)
• “Z” is a temperature coefficient which measures the
number of degrees required to change the D-value of
an organism by 1 log
Manufacture of sterile medicines –
25
Validation - Cycle Development
• The minimum Fo required by a sterilzation
process is related to the resistance of the
bioburden (D-value)
Fo = D121 (LogA - Log B)
where:
• “D121” is equal to the time at 121°C to reduce the
population of the most resistant organism in each
product container by 90% (or 1 log)
• “A” is the number of microoganisms per container
• “B” is the maximum acceptable probability of
survival (Sterility Assurance Level , 10-6
)
Manufacture of sterile medicines –
26
Validation - Cycle Development
• Two approaches to sterilization
– Overkill
– Probability of survival
• Overkill approach used when the product
can withstand excessive heat treatment
without adverse effects
– Cycle should deliver an Fo of at least 12
• This will achieve a 12 log reduction of
microorganisms with a D-value of 1 minute
(Assuming each product unit contains 106
organisms a 12 log
reduction will result in 10-6
organisms per unit or
probability of survival (SAL) of 1 in a million)
(Normal bioburden is usually much lower and the organisms
normally much less resistant than this)
Manufacture of sterile medicines –
27
Validation - Cycle Development
Biological Indicators
• device consisting of a known number of
microorganisms, of a known resistance to a
particular sterilization process in or on a carrier
and enclosed in a protective package.
– Organisms are in the form of endospores (not
vegetative state) as these are most resistant to
sterilization
Organism D-Value
Geobacillus stearothermophilus
(most common)
1 - 2.8
Bacillus coagulans 0.3
Clostridium sporogenes 0.8 – 1.4
Bacillus atropheus 0.5
Manufacture of sterile medicines –
28
Validation - Cycle Development
Spore Strips - a narrow strip of
fibrous paper impregnated with a
bacterial spore suspension
contained in a glassine envelope
Spore Dots - Circular pieces of
fibrous paper impregnated with
the spore suspension
Spore Suspensions - pure spore
suspension of the desired
challenge organism which can be
inocluated onto the surface of a
material
Self contained units containing spore
strips or suspensions and the
media in which they are to be
incubated (simple/convenient to
use)
Manufacture of sterile medicines –
29
Validation - Cycle Development
• Probability of Survival approach used used
for heat labile products
The process is validated to
achieve a destruction of the
presterilization bioburden to
a level of 100
(Point Y), with a
minimum safety factor of an
additional six-log reduction
(Point Z)
Determination of the
minimum Fo required is based
on the bioburden and its heat
resistance
What Fo would be required for a bioburden of 102
(100) if D-value was 1?
Manufacture of sterile medicines –
30
Validation of Sterilization
Basic Principles
• Installation Qualification (IQ)
– Ensuring equipment is installed as per
manufacturer’s specification
• Operation Qualification (OQ)
– Ensuring equipment, critical control equipment
and instrumentation are capable of operating
within required parameters
• Performance Qualifcation (PQ)
– Demonstrating that sterilizing conditions are
achieved in all parts of sterilization load
– Physical and microbiological
Manufacture of sterile medicines –
31
Validation - Equipment
Installation Qualification
• Ensuring equipment is installed as per
manufacturer’s specification
– considerations for new and existing equipment
– specifications for the type of autoclave,
construction materials, power supplies and
support services, alarm and monitoring
systems with tolerances and accuracy
requirements
– for existing equipment documented evidence
that the equipment can meet process
specifications
Manufacture of sterile medicines –
32
Validation - Equipment
Operational Qualification
• Ensuring equipment, critical control
equipment and instrumentation are capable
of operating within required parameters
• Three or more test runs which demonstrate
– controls, alarms, monitoring devices and operation
indicators function
– chamber pressure integrity is maintained
– chamber vacuum is maintained (if applicable)
– written procedures accurately reflect equipment operation
– pre-set operation parameters are attained for each run
Manufacture of sterile medicines –
33
Validation - Performance
Performance Qualification
• Demonstrating that sterilizing conditions are
achieved in all parts of sterilization load
• Physical and microbiological
Physical
• Heat distribution studies on empty chamber
– maximum and minimum cycle times and temperatures
– to identify heat distribution patterns including slowest
heating points
– mulitple temperature sensing devices should be used
(thermocouples)
– location of devices should be documented and ensure
that heat distribution is uniform
Manufacture of sterile medicines –
34
Validation - Performance
Performance Qualification - Physical (2)
• Heat distribution of maximum and minimum
chamber load configurations
– multiple thermocouples throughout chamber (not inside
product containers) to determine effect of load
configuration on temperature distribution
– temperature distribution for all loads using all container
sizes used in production should be tested
– position of thermocouples should be documented
– Slowest to heat/cold spots in each run should be
documented, inlcuding the drain
– repeat runs should be performed to check variability
– temperature distribution profile for each chamber load
configuration should be documented
Manufacture of sterile medicines –
35
Validation - Performance
Performance Qualification - Physical (3)
• Heat penetration studies to detect the maximum
and minimum temperature within all loads
– all parts of each load must be on contact with steam
– need to determine lowest and highest temperature
locations and slowest and fastest to heat locations
(measured inside product containers)
– need to consider all variables such as container size,
design, material, viscosity of solution and fill volume.
Container with maximum fill volume and slowest to heat
solution should be used
– maximum and minimum load configurations for each
sterilization cycle using routine cycle parameters
Manufacture of sterile medicines –
36
Validation - Performance
Performance Qualification - Physical (4)
• Heat penetration (2)
– May be necessary for container mapping for larger
volumes - cold spot then used for penetration studies
– Need to consider effects of packaging e.g. overwrapping
– Three runs performed once cold spots have been
identified to demonstrate reproducibility
Manufacture of sterile medicines –
37
Validation - Performance
Performance Qualification - Microbiological
• Biological challenge studies
– used when Probability of Survival approach is used
– may not be necessary when cycle is > 121°C for 15 minutes
(except US and Australia)
– biological indicators (BI) containing spores of Geobacillus
stearothermophilus are most commonly used (considered
“worst case”). BIs containing other organisms may be used
– performance studies based on product bioburden require a
considerable amount of work
– indicators should be placed throughout the load, adjacent to
thermocouples, at “cold spots” and slowest to heat locations
(identified during heat penetration studies)
– any growth is unacceptable unless processing errors
demonsrated
Manufacture of sterile medicines –
38
Validation - Performance
• Validation report must demonstrate requirements
in Validation protocol have been met, any
deviations must be justified
• Requalification must be repeated on an annual
basis (usually one run is acceptable)
• Any changes or modifications must be evaluated
– may just require requalification
– any changes to loading patterns, new container/closure
systems or cycle parameters require full validation
Manufacture of sterile medicines –
39
Routine Production
Issues considered for routine production
• Manufacturing environment should be controlled
• Procedures in place to minimize the pre-
sterilization bioburden
– bioburden limits specified (although not so important
when “overkill” cycle used)
• Time between filling and sterilization should be
specified
• Integrity of container/closure system should be
periodically verified
• Periodic leak testing of chamber (if vacuum is part
of cycle)
Manufacture of sterile medicines –
40
Routine Production
• Cooling water should be sterile
• Differentiation between sterilized and not-yet
sterilized product
– Physical separation (double ended autoclave)
– Labelling and use of visual indicators (e.g
autoclave tape)
• Periodic testing of containers to verify integrity of
container/closure system
• Quality of steam should be defined and
periodically tested for contaminants
Manufacture of sterile medicines –
41
Routine Production
• Each sterilization cycle must be monitored
– temperature, time and pressure recorded
– temperature recorder independent from cycle
controller
– second independent temperature recorder
– drain temperature should be recorded
– chemical and biololgical indicators (if
applicable)
• Sterilisation cycle records should form
part of batch records
Manufacture of sterile medicines –
42
Other Sterilization Processes
Sterilization using other processes should
follow a similar approach as that
described for moist heat
– Validation protocol
– Equipment calibration
– Determining the process that will deliver the
desired SAL (10-6
)
– IQ, OQ, PQ
– Requirements for routine monitoring and
control
Manufacture of sterile medicines –
43
Other Sterilization Processes
Dry Heat
– Should have air circulation in the chamber
– Positive pressure in the chamber to prevent
entry of non-sterile air
– HEPA filtered air supplied
– Biological indicators containing Bacillus
atropheus (if used)
• removal of endotoxin is usually sufficient
– When removing pyrogens need to validate
process using challenge tests
Manufacture of sterile medicines –
44
Other Sterilization Processes
Radiation
– Usually performed by contracting service
(need to ensure validation status,
responsibilities)
– Based on bioburden of product being
sterilised
• Biological indicators may be used as additional
control but may not be as resistant as naturally
occuring bioburden
– Method defined in International Standard ISO
11137
Manufacture of sterile medicines –
45
Other Sterilization Processes
Radiaton (2)
– Correct dose of radiation (~25 kGy) received by
all products (measured with dosimeters)
• quantitative measurement
• number, location, within calibration time-limit
– Radiation sensitive colour discs applied to
packaging
– procedures to distinguish irradiated and non-
irradiated materials
– Variation in density of packaging should be
addressed during validation
Manufacture of sterile medicines –
46
Other Sterilization Processes
Gasses and Fumigants
– e.g. ethylene oxide, hydrogen peroxide vapour
– Only when no other method is suitable
– Must demonstrate that process does not
adversely affect product
– Packaging must be able to permit ingress of
gas and humidity
– Ensure product load is adequately heated and
humidified prior to sterilization (called
“conditionning”)
• need to take into account validation performed in
summer or winter
Manufacture of sterile medicines –
47
Other Sterilization Processes
Gasses and Fumigants (2)
– Temperature distribution is acceptable
– Concentration of sterilant gas is sufficient
– Use of biological indicators is important
(Bacillus atropheus)
– Half cycles
• If cycle of half normal time destroys biological indicators
(106
organisms), double time will achieve SAL of 10-6
– Aeration
• Ventilated conditions
• Defined limits of residuals
• Process included in validation
– Safety and toxicity issues considered
Manufacture of sterile medicines –
48
Useful Publications
• ISO/EN 17665 - Sterilization of health care
products - Moist Heat (Parts 1 and 2)
• ISO/EN 11135 - Sterilization of health care
products - Ethylene Oxide (Parts 1 and 2)
• ISO/EN 11137 - Sterilization of health care
products - Radiation (Parts 1,2 and 3)
• “Validation of Moist Heat Sterilization Processes:
Cycle Design, Development, Qualification and
ongoing Control. PDA Technical Report No. 1
Revised 2007
Manufacture of sterile medicines –
49
Questions?

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1 2 sterilisation-validationqualification

  • 1. Manufacture of sterile medicines – 1 Sterilization - validation, qualification requirements Mrs Robyn Isaacson
  • 2. Manufacture of sterile medicines – 2 Sterilization - Overview Objectives – Discuss definition of “Sterile” – Briefly describe sterilization methods – Describe approaches to be used for the validation of a sterilization process using Moist Heat as an example – Describe requirements for routine monitoring and control of sterilization – Review issues that are specific to other sterilization processes
  • 3. Manufacture of sterile medicines – 3 Sterile Products - Overview • Certain pharmaceutical products must be sterile – injections, ophthalmic preparations, irrigations solutions, haemodialysis solutions • Two categories of sterile products – those that can be sterilised in final container (terminally sterilised) – those that cannot be terminally sterilised and must be aseptically prepared
  • 4. Manufacture of sterile medicines – 4 Sterilization - Overview What is the definition of “sterile”? • Free from microorganisms In practice no such absolute statement regarding absence of microorganisms can be proven • Defined as the probability of 1 in a million of a container being contaminated (10-6 ) • This referred to as the Sterility Assurance Level (SAL) • Organisms are killed in an exponential fashion
  • 5. Manufacture of sterile medicines – 5 Definition of “Sterile” MICROBIAL INACTIVATION Nt = Noe -kt 0 200 400 600 800 1000 1200 Time Noofsurvivingorganisms -2.00 -1.50 -1.00 -0.50 0.00 0.50 1.00 1.50 2.00 2.50 3.00 3.50 No remaining Log No remaining No remaining 1000 368 135 50 18 7 2 1 0 0 0 Log No remaining 3.00 2.57 2.13 1.70 1.26 0.83 0.39 -0.04 -0.47 -0.91 -1.34 0 1 2 3 4 5 6 7 8 9 10
  • 6. Manufacture of sterile medicines – 6 Definition of “Sterile” Microbial Inactivation -3 -2 -1 0 1 2 3 4 1 2 3 4 5 6 Time LogNoofSurvivingOrganisms D-value - Time (or dose) required to reduce the population of organisms by 1 log (or 90%) D-Value Resistance of an organism is referred as its “D-value”
  • 7. Manufacture of sterile medicines – 7 Definition of “Sterile” • A sterilization process must deliver a Sterility Assurance Level (SAL) of 1 in a million (10-6 ) • It is not possible to measure “10-6 ” • The required SAL can be achieved by applying a process that will reduce the number of organisms to zero and then apply a safety factor that will deliver an extra 6 log reduction
  • 8. Manufacture of sterile medicines – 8 Definition of “Sterile” Example • For an initial bioburden of 102 the sterilization process will need to achieve an 8 log reduction in viable organisms • This will require 8 times the D- value (e.g. if the organism has a D value of 2 minutes then 8 x 2 = 16 minutes will be required to achieve an 8 log reduction and an SAL of 10-6 ) (Point Z) Microbial Death Curve -7 -6 -5 -4 -3 -2 -1 0 1 2 0 1 2 3 4 5 6 7 8 Time LogNoofSurvivors Y Z
  • 9. Manufacture of sterile medicines – 9 Sterilization - Overview Commonly used methods of sterilization – Moist Heat – Dry Heat – Gas (Ethylene oxide) – Radiation (Gamma or Electron) – Filtration – Others - UV, Steam and formaldehyde, hydrogen peroxide
  • 10. Manufacture of sterile medicines – 10 Moist Heat • Saturated steam • Common cycles: – 121°C for 15 minutes – 134°C for 3 minutes – Other cycles of lower temperature and longer time may be used (e.g. 115°C for 30 minutes) • Used for sterilization of: – terminal sterilization of aqueous injections, ophthalmic preparations, irrigation & haemodialysis solutions, equipment used in aseptic processing
  • 11. Manufacture of sterile medicines – 11 Moist Heat • not suitable for non-aqueous/dry preparations • preferred method of sterilization
  • 12. Manufacture of sterile medicines – 12 Dry Heat • Lethality due to oxidative processes • Higher temperatures and longer exposure times required • Typical cycles: – 160°C for 120 minutes – 170°C for 60 minutes – 180°C for 30 minutes – tunnels used for the sterilisation of glass vials may use much higher temperatures (300°) for a much shorter period
  • 13. Manufacture of sterile medicines – 13 Dry Heat • Used for: – glassware and product containers used in aseptic manufacture, non aqueous thermostable powders and liquids (oils) • also used for depyrogenation of glassware (≥250°C) – (Pyrogens - substances found in cell wall of some bacteria which can cause fever when introduced into the body)
  • 14. Manufacture of sterile medicines – 14 Ethylene Oxide Gas • Either pure or in mixtures with other inert gases • Requires presence of moisture • Complex process • Typical cycles: – 1-24hours – 25-1200 mg/L gas – 25-65°C – 30-85% relative humidity
  • 15. Manufacture of sterile medicines – 15 Ethylene Oxide • Used for: – heat labile product containers – surface sterilization of powders • Adequate aeration to reduce toxic residues
  • 16. Manufacture of sterile medicines – 16 Radiation • Gamma rays generated by Cobalt 60 or Caesium 137 radionuclides; or • Accelerated electrons from an electron generator • 25 kilograys (kGy) usual dose – dose dependent on bioburden (resistance of organisms not predictable) • process must be properly validated • used for: – dry pharmaceutical products – heat labile product containers • can cause unacceptable changes
  • 17. Manufacture of sterile medicines – 17 Filtration • Removes organisms from liquids and gasses • 0.2 - 0.22 micron for sterilization • composed of cellulose esters or other polymeric materials • filter material must be compatible with liquid being filtered • used for bulk liquids, gasses and vent filters
  • 18. Manufacture of sterile medicines – 18 Validation - Overview • Selection of sterilzation process must be appropriate for product – terminal sterilization is the method of choice – moist heat (autoclaving) is the most common process used for terminal sterilization – product must not be affected by heat – container/closure integrity must be established – items being sterilised must contain water (if sealed) or material must allow for removal of air and penetration of steam for steam (moist heat) sterilization
  • 19. Manufacture of sterile medicines – 19 Validation - Protocol Requirements for Moist Heat Sterilization Other processes follow similar requirements • Validation protocol should include the following details for each sterilization process – process objectives in terms of product type, container/closure system, SAL required – specifications for time, temperature, pressure and loading pattern – description of all equipment and support systems in terms of type, model, capacity and operating range
  • 20. Manufacture of sterile medicines – 20 Validation - Protocol Moist Heat continued: – performance characteristics of all equipment e.g. pressure gauges, valves, alarm systems, timers, steam flow rates/pressures, cooling water flow rates, cycle controller functions, door closure gasketing and air break systems and filters – methodology for monitoring performance of equipment and the process and labatory testing methodology – personnel responsible for all stages and final evaluation (should have experience and necessary training and be authorized)
  • 21. Manufacture of sterile medicines – 21 Validation - Calibration • Laboratory testing should be performed by a competent laboratory, methodology should be documented • All instruments must be calibrated e.g. – temperature recorders and sensors – thermocouples – pressure sensors for jacket and chamber – timers – conductivity monitors for cooling water – flow metres for water/steam – water level indicators when cooling water is used – thermometers including those for thermocouple reference, chamber monitoring and laboratory testing
  • 22. Manufacture of sterile medicines – 22 Validation - Calibration • Indicators should be calibrated – physical and chemcial indicators should be tested to demonstrate acceptable response to time and temperature – biological indicators should be tested for count and time/temperature exposure response • for commercial indicators - test certificate with count and D-value and exposure response should be available. Results acceptable if verified “in house” periodically. • In house indicators must be fully characterized (D- value, identification) and appropriate for sterilization process All indicators should be appropriately stored and within expiry
  • 23. Manufacture of sterile medicines – 23 Validation - Cycle Development • Concept of Fo – Lethality factor equivalent to time at 121°C • 1 minute at 121°C is equivalent to Fo of 1. • Lethality can accumulate during heat up and cool down phases Typical temperature profile of a heat sterilization process What would be the Fo of a cycle at 121°C for 15 minutes?
  • 24. Manufacture of sterile medicines – 24 Validation - Cycle Development • Fo is calculated using the following equation: Fo = ΔtΣ10(T-121/Z) where: • “Δt” is the time interval between measurements of temperature (T) • “T” is the temperature of sterilised product at time (t) • “Z” is a temperature coefficient which measures the number of degrees required to change the D-value of an organism by 1 log
  • 25. Manufacture of sterile medicines – 25 Validation - Cycle Development • The minimum Fo required by a sterilzation process is related to the resistance of the bioburden (D-value) Fo = D121 (LogA - Log B) where: • “D121” is equal to the time at 121°C to reduce the population of the most resistant organism in each product container by 90% (or 1 log) • “A” is the number of microoganisms per container • “B” is the maximum acceptable probability of survival (Sterility Assurance Level , 10-6 )
  • 26. Manufacture of sterile medicines – 26 Validation - Cycle Development • Two approaches to sterilization – Overkill – Probability of survival • Overkill approach used when the product can withstand excessive heat treatment without adverse effects – Cycle should deliver an Fo of at least 12 • This will achieve a 12 log reduction of microorganisms with a D-value of 1 minute (Assuming each product unit contains 106 organisms a 12 log reduction will result in 10-6 organisms per unit or probability of survival (SAL) of 1 in a million) (Normal bioburden is usually much lower and the organisms normally much less resistant than this)
  • 27. Manufacture of sterile medicines – 27 Validation - Cycle Development Biological Indicators • device consisting of a known number of microorganisms, of a known resistance to a particular sterilization process in or on a carrier and enclosed in a protective package. – Organisms are in the form of endospores (not vegetative state) as these are most resistant to sterilization Organism D-Value Geobacillus stearothermophilus (most common) 1 - 2.8 Bacillus coagulans 0.3 Clostridium sporogenes 0.8 – 1.4 Bacillus atropheus 0.5
  • 28. Manufacture of sterile medicines – 28 Validation - Cycle Development Spore Strips - a narrow strip of fibrous paper impregnated with a bacterial spore suspension contained in a glassine envelope Spore Dots - Circular pieces of fibrous paper impregnated with the spore suspension Spore Suspensions - pure spore suspension of the desired challenge organism which can be inocluated onto the surface of a material Self contained units containing spore strips or suspensions and the media in which they are to be incubated (simple/convenient to use)
  • 29. Manufacture of sterile medicines – 29 Validation - Cycle Development • Probability of Survival approach used used for heat labile products The process is validated to achieve a destruction of the presterilization bioburden to a level of 100 (Point Y), with a minimum safety factor of an additional six-log reduction (Point Z) Determination of the minimum Fo required is based on the bioburden and its heat resistance What Fo would be required for a bioburden of 102 (100) if D-value was 1?
  • 30. Manufacture of sterile medicines – 30 Validation of Sterilization Basic Principles • Installation Qualification (IQ) – Ensuring equipment is installed as per manufacturer’s specification • Operation Qualification (OQ) – Ensuring equipment, critical control equipment and instrumentation are capable of operating within required parameters • Performance Qualifcation (PQ) – Demonstrating that sterilizing conditions are achieved in all parts of sterilization load – Physical and microbiological
  • 31. Manufacture of sterile medicines – 31 Validation - Equipment Installation Qualification • Ensuring equipment is installed as per manufacturer’s specification – considerations for new and existing equipment – specifications for the type of autoclave, construction materials, power supplies and support services, alarm and monitoring systems with tolerances and accuracy requirements – for existing equipment documented evidence that the equipment can meet process specifications
  • 32. Manufacture of sterile medicines – 32 Validation - Equipment Operational Qualification • Ensuring equipment, critical control equipment and instrumentation are capable of operating within required parameters • Three or more test runs which demonstrate – controls, alarms, monitoring devices and operation indicators function – chamber pressure integrity is maintained – chamber vacuum is maintained (if applicable) – written procedures accurately reflect equipment operation – pre-set operation parameters are attained for each run
  • 33. Manufacture of sterile medicines – 33 Validation - Performance Performance Qualification • Demonstrating that sterilizing conditions are achieved in all parts of sterilization load • Physical and microbiological Physical • Heat distribution studies on empty chamber – maximum and minimum cycle times and temperatures – to identify heat distribution patterns including slowest heating points – mulitple temperature sensing devices should be used (thermocouples) – location of devices should be documented and ensure that heat distribution is uniform
  • 34. Manufacture of sterile medicines – 34 Validation - Performance Performance Qualification - Physical (2) • Heat distribution of maximum and minimum chamber load configurations – multiple thermocouples throughout chamber (not inside product containers) to determine effect of load configuration on temperature distribution – temperature distribution for all loads using all container sizes used in production should be tested – position of thermocouples should be documented – Slowest to heat/cold spots in each run should be documented, inlcuding the drain – repeat runs should be performed to check variability – temperature distribution profile for each chamber load configuration should be documented
  • 35. Manufacture of sterile medicines – 35 Validation - Performance Performance Qualification - Physical (3) • Heat penetration studies to detect the maximum and minimum temperature within all loads – all parts of each load must be on contact with steam – need to determine lowest and highest temperature locations and slowest and fastest to heat locations (measured inside product containers) – need to consider all variables such as container size, design, material, viscosity of solution and fill volume. Container with maximum fill volume and slowest to heat solution should be used – maximum and minimum load configurations for each sterilization cycle using routine cycle parameters
  • 36. Manufacture of sterile medicines – 36 Validation - Performance Performance Qualification - Physical (4) • Heat penetration (2) – May be necessary for container mapping for larger volumes - cold spot then used for penetration studies – Need to consider effects of packaging e.g. overwrapping – Three runs performed once cold spots have been identified to demonstrate reproducibility
  • 37. Manufacture of sterile medicines – 37 Validation - Performance Performance Qualification - Microbiological • Biological challenge studies – used when Probability of Survival approach is used – may not be necessary when cycle is > 121°C for 15 minutes (except US and Australia) – biological indicators (BI) containing spores of Geobacillus stearothermophilus are most commonly used (considered “worst case”). BIs containing other organisms may be used – performance studies based on product bioburden require a considerable amount of work – indicators should be placed throughout the load, adjacent to thermocouples, at “cold spots” and slowest to heat locations (identified during heat penetration studies) – any growth is unacceptable unless processing errors demonsrated
  • 38. Manufacture of sterile medicines – 38 Validation - Performance • Validation report must demonstrate requirements in Validation protocol have been met, any deviations must be justified • Requalification must be repeated on an annual basis (usually one run is acceptable) • Any changes or modifications must be evaluated – may just require requalification – any changes to loading patterns, new container/closure systems or cycle parameters require full validation
  • 39. Manufacture of sterile medicines – 39 Routine Production Issues considered for routine production • Manufacturing environment should be controlled • Procedures in place to minimize the pre- sterilization bioburden – bioburden limits specified (although not so important when “overkill” cycle used) • Time between filling and sterilization should be specified • Integrity of container/closure system should be periodically verified • Periodic leak testing of chamber (if vacuum is part of cycle)
  • 40. Manufacture of sterile medicines – 40 Routine Production • Cooling water should be sterile • Differentiation between sterilized and not-yet sterilized product – Physical separation (double ended autoclave) – Labelling and use of visual indicators (e.g autoclave tape) • Periodic testing of containers to verify integrity of container/closure system • Quality of steam should be defined and periodically tested for contaminants
  • 41. Manufacture of sterile medicines – 41 Routine Production • Each sterilization cycle must be monitored – temperature, time and pressure recorded – temperature recorder independent from cycle controller – second independent temperature recorder – drain temperature should be recorded – chemical and biololgical indicators (if applicable) • Sterilisation cycle records should form part of batch records
  • 42. Manufacture of sterile medicines – 42 Other Sterilization Processes Sterilization using other processes should follow a similar approach as that described for moist heat – Validation protocol – Equipment calibration – Determining the process that will deliver the desired SAL (10-6 ) – IQ, OQ, PQ – Requirements for routine monitoring and control
  • 43. Manufacture of sterile medicines – 43 Other Sterilization Processes Dry Heat – Should have air circulation in the chamber – Positive pressure in the chamber to prevent entry of non-sterile air – HEPA filtered air supplied – Biological indicators containing Bacillus atropheus (if used) • removal of endotoxin is usually sufficient – When removing pyrogens need to validate process using challenge tests
  • 44. Manufacture of sterile medicines – 44 Other Sterilization Processes Radiation – Usually performed by contracting service (need to ensure validation status, responsibilities) – Based on bioburden of product being sterilised • Biological indicators may be used as additional control but may not be as resistant as naturally occuring bioburden – Method defined in International Standard ISO 11137
  • 45. Manufacture of sterile medicines – 45 Other Sterilization Processes Radiaton (2) – Correct dose of radiation (~25 kGy) received by all products (measured with dosimeters) • quantitative measurement • number, location, within calibration time-limit – Radiation sensitive colour discs applied to packaging – procedures to distinguish irradiated and non- irradiated materials – Variation in density of packaging should be addressed during validation
  • 46. Manufacture of sterile medicines – 46 Other Sterilization Processes Gasses and Fumigants – e.g. ethylene oxide, hydrogen peroxide vapour – Only when no other method is suitable – Must demonstrate that process does not adversely affect product – Packaging must be able to permit ingress of gas and humidity – Ensure product load is adequately heated and humidified prior to sterilization (called “conditionning”) • need to take into account validation performed in summer or winter
  • 47. Manufacture of sterile medicines – 47 Other Sterilization Processes Gasses and Fumigants (2) – Temperature distribution is acceptable – Concentration of sterilant gas is sufficient – Use of biological indicators is important (Bacillus atropheus) – Half cycles • If cycle of half normal time destroys biological indicators (106 organisms), double time will achieve SAL of 10-6 – Aeration • Ventilated conditions • Defined limits of residuals • Process included in validation – Safety and toxicity issues considered
  • 48. Manufacture of sterile medicines – 48 Useful Publications • ISO/EN 17665 - Sterilization of health care products - Moist Heat (Parts 1 and 2) • ISO/EN 11135 - Sterilization of health care products - Ethylene Oxide (Parts 1 and 2) • ISO/EN 11137 - Sterilization of health care products - Radiation (Parts 1,2 and 3) • “Validation of Moist Heat Sterilization Processes: Cycle Design, Development, Qualification and ongoing Control. PDA Technical Report No. 1 Revised 2007
  • 49. Manufacture of sterile medicines – 49 Questions?