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    Comparing the Manufactureand Use of Closed andOpen mpoules forManufacture ParenteralProducts Using FMECharles S. Levine

    VPCI

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    Closed vs. Openampoules

    Open Washed

    Depyrogenated

    Filled Flame sealed

    Terminally

    sterilized

    Closed Externally

    sterilized

    Opened

    mechanically or

    by flame

    Filled

    Flame sealed

    Terminally

    sterilized

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    Supplier Manufacturer

    Cooperation

    Drug Product Manufacturer

    Sintetica S.A., Lugano, Switzerland

    Ampoule Manufacturer

    AR.LA.VE.S. s.r.l. (AritcoliLavorazione Vetro Soffiato),

    Treviglio (BG) Italy

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    Supplier ManufacturerCooperation

    Mutual Goals Improved quality of Ampoules

    Improved quality of Drug Product Reduced scrap during Drug Product

    Manufacturing

    Potential for expanded markets forClosed Ampoules

    Potential for expanded markets for

    Drug Products manufactured usingClosed Ampoules

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    Does the use of ClosedAmpoules Benefit the

    Patient?

    Maintains high Quality Standards

    while minimizing Capitalexpenditures, which aids in the

    control of drug prices.

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    Presentation outline

    Risk analysis technique

    Analysis of Ampoule formation process

    Analysis of drug product manufacturing

    process

    Summary of process enhancements

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    HACCP

    Conduct a hazard analysis Determine the critical control points

    Establish critical limits

    Establish monitoring procedures

    Establish corrective action

    Establish verification plan

    Establish recordkeeping and

    documentation procedures J.G. Surak, HACCP and ISO development of a food is safety management standard, ASQ, FDC Control, No.135, 2003.

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    Controlling Risk

    At each critical control point identify theappropriate method for controlling

    product quality.

    100% inspection Automated

    Manual

    Equipment controllers Process validation

    Periodic sampling and inspection

    Finished product testing

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    FMEA

    FMEA (Failure Mode and Effects Analysis) isa systematic method of identifying and

    preventing product and process problemsbefore they occur.*

    R. E. McDermott, The Basics of FMEA, 1996

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    FMEA process Define the process

    Select a team of experts Develop the FMEA matrix

    Process function

    Failure mode

    Failure effects Failure causes

    Probability of failure

    Severity of effects

    Likelihood of detection Calculate Risk Priority Number (RPN)

    Take preventive and corrective action

    Recalculate RPN A. Sahni, Using Failure Mode and Effects Analysis to Improve Manufacturing Processes,1993

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    FMEA

    Failure mode presence of foreign particulate

    matter

    Cause of failure

    Inadequate control of environmental

    conditions during the formation ofthe ampoules

    Failure effect

    Potential injury to the patient

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    Calculation of Risk

    Priority Number (RPN)

    RPN = P X S X D Where

    P = Probability of Failure

    S = Severity (Potential harm to patient)

    D = Likelihood of detection

    For each variable Scaled from 1 to 5

    1 is best case

    5 is Worst case

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    Probability of Failure

    (P)

    P = 5 failure will occur

    often

    P = 1 unlikely to occur

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    Severity (S)

    S= 5 serious injury to the patient

    or employee or high cost to thecompany

    S= 1 no effect on the patient oremployee

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    Likelihood of Detection

    (D) D = 5 No method to detect Failure

    D = 1 Failure is immediatelydetectable

    Applications of FMEA in the Pharmaceutical Industry, Pharmaceutical Technology, R. Kieffer

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    Drug Product

    Manufacturing ProcessDescription

    Product Epinephrine 1mg/ml (1ml in a 2ml Ampoule)

    Glass Type I Flint

    Filling process Clean Fill (not aseptic)

    Sterilization

    Terminally sterilized (overkill cycle)

    Leak test Vacuum Hold

    100% inspection Automated

    Wh t i th diff

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    What is the difference

    between a Closed and

    Open Ampoule?

    Sealed during transport andpreparation for delivery into Filling area

    Sealed at the glass manufacturer with

    a slight overpressure

    The internal surfaces of the ampoule

    are not cleaned or depyrogenated atthe Drug Product manufacturer

    Process Control shifts from the Drug

    Product manufacturer to the Glassmanufacturer

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    Risk Analysis Objective

    Minimize the risk that the use of

    Closed Ampoules versus OpenAmpoules increases the risk of

    foreign particulate matter.

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    Analyzing Risk

    Ampoule Forming Process

    Establish risk assessment team

    Osiris Donghi, Technical Director,ARLAVES

    Sergio Randisi, Director QA, ARLAVES

    Augusto Mitidieri, Director QA, Sintetica

    Charles Levine, Consultant, VPCI

    Detailed process definition

    Identify potential hazards and critical control

    points

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    Analyzing Risk Drug

    Product ManufacturingProcess Establish risk assessment team

    E. Giudice, Production Supervisor,

    Sintetica

    B. Ricardi, Manager QA, Sintetica

    N. Caronzolo, Manager QC, Sintetica

    A. Angelini, Qualified Person, Sintetica

    A. Mitidieri, General Manager, Sintetica

    C. Levine, consultant, VPCI

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    Closed Ampoule FormingProcess (2003)

    Ampoules are formed and cut from the glasstubing

    The ampoules exit the forming machine as

    open ampoules Cooled from approximately 300C to ambient

    temperature

    Score break Station

    Ampoule Chilling (approximately 4C)

    Ampoule sealing station

    Ampoule annealing oven

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    Ampoule annealing

    oven Heating phase

    140 to 590C Cooling phase

    590 to 70C

    Bacterial endotoxin reduction

    3 log

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    Ampoule Forming Line

    CLevine_info.pdf

    http://i/PROGRAMS%20&%20MEETINGS%20DEPARTMENT/2005%20Meetings/Rome%202005/Presentations/Web%20Presentations/CLevine_info.pdfhttp://i/PROGRAMS%20&%20MEETINGS%20DEPARTMENT/2005%20Meetings/Rome%202005/Presentations/Web%20Presentations/CLevine_info.pdfhttp://i/PROGRAMS%20&%20MEETINGS%20DEPARTMENT/2005%20Meetings/Rome%202005/Presentations/Web%20Presentations/CLevine_info.pdf
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    Supplier of Type I

    Glass Tubing Schott Rohrglas, Bayreuth,

    Germany Kimble Italiana, Montelungo, Italy

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    Tubing Specifications

    Densocan tubing from Schott

    Length 1500 mm

    Sealed at both ends with a vent hole(>0.5mm)

    Glass Particle specification (sampleselection according to ANSI/ASQC z1.4 1993/DIN ISO 2859-1, simple randomsample, test level II, normal test

    Particle size ( 0.2 0.5 mm)

    Maximum number of particles 4

    AQL 0.65

    Particle size (>0.5 mm) Maximum number of particles 1

    AQL 0.65

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    Tubing Performance

    20 ampoules are produced fromeach 1.5m tube

    20mm at each end of the tube areautomatically discarded

    The tubing is heated to 1200oC to

    form ampoules

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    Self Ignition

    Temperatures Polyvinyl Chloride - 507oC

    Polyethylene - 488oC

    Cellulose - 260oC

    National Fire Protection Association (NFPA)

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    Higher Risk Process

    Steps

    Transporting open ampoules to the cooling

    tunnel (RPN=18 ) Filtration of the air supplied to the cooling

    tunnel (RPN=12 )

    Filtration of the air at the refrigeration Station(RPN=12 )

    Proximity of the score brake station to theampoule sealing station (RPN=24 )

    Control of the vacuum level at the score brakestation (RPN=12 )

    Maximum possible value of RPN is 125

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    Critical Control Points Process step

    Transporting openampoules to the coolingtunnel

    Filtration of the airsupplied to the cooling

    tunnel Filtration of the air at the

    refrigeration Station

    Proximity of the scorebrake station to theampoule sealing station

    Control of the vacuumlevel at the score brakestation

    Critical control point

    None

    Roughing filters only

    Roughing filters only

    None

    None

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    Corrective Actions Process step

    Transporting openampoules to the coolingtunnel

    Filtration of the airsupplied to the cooling

    tunnel Filtration of the air at the

    refrigeration Station

    Proximity of the scorebrake station to theampoule sealing station

    Control of the vacuumlevel at the score brakestation

    Corrective Action

    Install protective barrier

    Install F8 (EN779) filters

    Install F8 (EN779) filters

    Relocate score brakestation and installseparation barrier

    Install low vacuum alarm

    Recalculation of RPN

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    Recalculation of RPN

    Ampoule Forming Process

    612Control of the vacuum level at the

    score brake station

    624Proximity of the score brake stationto the ampoule sealing station

    612Filtration of the air at the refrigeration

    Station

    612Filtration of the air supplied to the

    cooling tunnel

    1218Transporting open ampoules to the

    cooling tunnel

    RPN (2004)RPN (2003)Process step

    Closed Ampoule

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    Closed Ampoule

    Manufacturing Process(2004)

    Ampoules are formed and cut from the glasstubing

    Ampoules are transported in a protectivebarrier

    Cooled from approximately 300C to ambienttemperature with F8 filtered air

    Ampoule Chilling (approximately 4C) with F8filtered air

    Ampoule sealing station Score break (vacuum system equipped with

    low level alarm)

    Ampoule annealing oven

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    Ampoule forming Line

    1- Cooling Tunnel (openAmpoules)

    2- Refrigerated Air (coolAmpoules to 4oC)

    3- Ampoule SealingStation

    4- Transport Belt(Closed Ampoules)

    5 Vacuum ControlSystem

    6- Score Break Station1 2 3 4 65

    D P d t

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    Drug Product

    Manufacturing Process(2003)

    Receive and release of ampoules

    Prepare ampoules for clean room

    filling process Prepare drug product solution

    Fill ampoules Terminally sterilize drug product

    100% inspection

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    Prepare Ampoules forClean Room Filling

    Process

    Remove plastic wrap from

    modules Reject any damaged modules

    Autoclave ampoules in a doubledoor jacketed steam autoclave

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    Fill Ampoules

    Visually inspect each tray of ampoules

    for defective ampoules The filling system automatically

    opens the ampoule (inverted)

    Fills the drug product

    Seals the ampoule

    Visually inspect each tray of filledampoules for defective seals

    Periodically remove samples for fillvolume, seal dimensions and cosmeticinspection

    T i ll St ili D

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    Terminally Sterilize Drug

    Product

    Load the ampoules in the invertedorientation

    Overkill sterilization cycle at 121oC Post-vacuum hold cycle (leak test)

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    100% inspection

    Automated inspection for

    Low Fill Volume (leakers) Particulate matter

    Hi h Ri k P

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    Higher Risk Process

    Steps Opening ampoules (generation of

    glass particles) (RPN= 18)

    Filling ampoules in a Class C

    environment Airborne particles related to facility

    design (RPN=12)

    Airborne particles related to

    personnel gowning (RPN=18 )

    Ampoule leak test (RPN=10 )

    C iti l C t l P i t

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    Critical Control Points

    Process Step

    Opening ampoules

    (generation of glassparticles)

    Filling ampoules in aClass C

    environment Airborne particles

    related to facilitydesign

    Airborne particlesrelated to personnelgowning

    Ampoule leak test

    Critical ControlPoint

    Exhaust Interlock

    Monitoring P

    Change FillingRoom OperatorsClothing daily

    Cycle Review

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    Corrective Actions Process Step Opening ampoules

    (generation of glassparticles)

    Filling ampoules in aClass C environment

    Airborne particles

    related to facilitydesign

    Airborne particlesrelated to personnel

    gowning Ampoule leak test

    Corrective Actions Validate interlock

    Increase Environmental

    Monitoring Frequency

    Convert to single-usedisposable gowns

    Trend PM rejects

    Demonstrate sensitivityof leak test (Validation)

    Recalculation of RPN

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    Recalculation of RPN

    Drug Product Manufacture

    510Ampoule leak test

    1218Airborne particles related to

    personnel gowning

    612Airborne particles related to

    facility design

    1218Opening ampoules

    (generation of glassparticles)

    RPN (2004)RPN (2003)Process step

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    Ampoule Leak Test

    Process

    140 minutes at 0.2 Bar (Inverted

    Orientation) 100% automated fill volume

    inspection

    A l L k T t

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    Ampoule Leak Test

    Validation

    Establish Fill Volume Sensitivity Label Claim 1.0ml

    Challenged with ampoules filledwith

    0.80ml

    0.90ml

    0.95ml

    10 of 10 rejected with 0.95ml

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    Ampoule Leak Test

    Validation

    Create 20 ampoules each withholes using Lasers

    10m 20m

    30m

    Ampoules with 10m were empty

    after the leak test cycle

    Particulate Matter

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    Reject History

    0412490.2%26213237104069

    030537

    041249

    0.9%118713025704068

    0305370.9%1217128676040670302500.8%2933559903122

    0305370.8%110412998503168

    0305370.7%90212968803167

    0305370.6%74012946103166

    0302507%742811186103099

    030227

    030250

    6%8225128151030980302274%477912557003097

    Ampoules

    Lot No.%

    N particulate

    matter rejects

    Number

    InspectedBatch No.

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    Customer Complaint

    Frequency

    No Complaints received for

    particulate matter

    S

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    Summary

    FMEA is a tool that can identify

    those processes that represent thegreatest risk for failures of various

    types.

    FMEA is also a tool that can

    evaluate an overall control

    program to ensure that limitedquality resources are being utilized

    in the most cost-effective manner.

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    Grazie per Tutti

    Augusto Mitidieri, General Manager,

    Sintetica, S.A. Osiris Donghi, Technical Director,

    ARLAVES

    Sergio Randisi, Director QA, ARLAVES

    Franco DeVecchi, VPCI