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TechnicalReportNo.77
TheManufactureofSterilePharmaceutical
ProductsUsingBlow-Fill-SealTechnology
PDATheManufactureofSterilePharmaceuticalProductsUsingBlow-Fill-SealTechnology
TechnicalReportTeam
Authors
MartinHaerer,HolopackVerpackungstechnik,TeamCo-leader(BFSIOA)
KennethMuhvich,Micro-Reliance,LLC,TeamCo-leader(PDA)
PeterAkerman,AstraZeneca
JaimeBlanco,Genentech
NerminCchajic,KemPharm,Inc.
KevinDowney,TevaPharmaceutical
TyDuginske,Baxter
AndrewGoll,WeilerEngineering,Inc
TimKram,RommelagUSA,Inc.
StaceyLargent,Merck
JesperLaursen,MELITEKA/S
MattPayne,RitedoseCorporation
PatrickPoisson,UnitedTherapeutics
ChuckReed,ReedsandRushes,LLC
OttoSchubert,MaropackAG
JerryWebb,NephronPharmaceuticalCorporation
TheManufactureofSterile
PharmaceuticalProductsUsingBlow-Fill-Seal
Technology
TechnicalReportNo.77
ISBN:978-0-939459-94-0
◎2017ParenteralDrugAssociation,Inc.Allrightsreserved.
ThistechnicalreportwasdevelopedandwrittenincooperationwiththeBlow-Fill-SealInternationalOperators
Association(BFSIOA).Thecontentandviewsexpressedinthistechnicalreportaretheresultofaconsensus
achievedbythePDAauthoringtaskforceandarenotnecessarilyviewsoftheorganizationstheyrepresent.
TableofContents
1.0INTRODUCTION
1
1.1Purpose
1
12Scope
1
1.3BFSProcessOutline
1
2.0GLOSSARYOFTERMS
3
2.1Abbreviations
3
3.0BFSEQUIPMENT
3
3.1ShuttleTypeMachines
(0penParisonProcess)
3
3.2RotaryFilingMachines(ClosedPanisonProcess) 4
3.3AdditionalApplications
5
4.0BENEFITS&SPECIALCONSIDERATIONSOFBFS
TECHNOLOGY
6
4.1Benefits
7
4.2SpecialConsiderations
7
5.0DESIGN
8
5.1ProductDesign
8
5.1.1AsepticProcessingversusTerminal
Sterilization
8
5.1.2TerminalSterilization
8
5.1.3Polymer
9
5.1.4ProductApplications
9
5.1.5ContainerDesign
10
5.1.6SecondaryPackaging
10
5.2EquipmentDesign
10
5.2.1General
10
5.2.2ProductPathway
11
5.2.3MoldDesign
11
5.2.4VacuumSystem
11
5.2.5Deflashing
12
5.2.6EquipmentMonitoring
12
5.3FacilityDesign
12
5.3.1AsepticProcessingArea
12
5.3.2PolymerStorageandDistribution
12
5.3.3Utilities
13
6.0OPERATIONALANDQUALIFICATION
CONSIDERATIONS
13
6.1BFSProcessValidationandAdvanced
Technology
13
forQualityandSterility
14
6.2EvaluatingCriticalBFSProcessParameters
6.3QualityAttributeCriticalProcessParameters 15
6.3.1AirFlowRate
15
6.3.2MainMoldVacuumDelayTimer
15
6.3.3BottleBlowingTimer
15
6.3.4SealMoldVacuumDelayTimer
16
6.4SterilityAssurance-relatedCriticalProcess
Parameters
16
6.4.1FillNozzleDownDelayTimer
16
6.4.2BottleBlowingTimer
16
6.4.3BottleVentTimer
16
6.4.4MasterFillTimer
16
6.4.5IndividualFillTimers
16
6.4.6FillNozzleUpDelayTimer
16
6.5Implementation
16
6.6Pre-processPreparationofCriticalAreas 17
6.6.1SanitizationofMachineSurfaces
17
6.6.2CleaningofProductContactSurfaces
17
6.6.3SterilizationofProductPathway
18
6.7ProductValidation
18
6.7.1ContainerClosureIntegrityTesting
18
6.7.2LeakDetection
19
6.7.3CampaignFill/HoldingTime
19
6.7.4In-ProcessSampling
19
6.8EquipmentValidation
19
6.8.1CriticalZoneControl
19
6.8.2AirShowerDesign(OpenParison
Machines)
20
6.8.3BFSMachineRoomEnvironment
20
6.8.4FiltrationConfiguration
20
6.8.5FilterIntegrity
20
6.8.6Air/GasFiltration
20
6.8.7AsepticCompoundingandOtherPre-BFS
ProductSteriizationApproaches
21
6.8.8EnvironmentalMonitoring
21
BFSShuttleMachines
21
BFSRotaryMachines 22
6.8.9ExtrusionConsiderations 22
6.8.10Controls 22
6.8.11DownstreamProcess 22
6.9ProcessSimulation(MediaFill)forAseptic
FillingLines 22
6.9.1Design 22
6.9.2Interventions 23
6.10Gowning 24
6.11FacilityValidation 24
7.0QUALITYRISKASSESSMENT 24
7.1ProductContamination 25
8.0REFERENCES 26
9.0APPENDIXI:EXAMPLEOFAQUALITYRISK
ASSESSMENT 28
10.0APPENDIXII:ENVIRONMENTALPARTICLE
MONITORINGLEVELS 32
FIGURESANDTABLESINDEX
Figure3.1-1
Figure3.2-1
Figure3.2-2
Table5.1.3-1
Table5.1.5-1
Figure6.2-1
Table6.5-1
Table7.2-1
Table7.2-2
DiagrammaticRepresentationofthe
OpenParisonBFSProcess
4
RotaryBFSMachineSchematic
5
BFSProcessDetailforRotary
Machines
6
ParametersforAssessingPolymer
Selection
9
ContainerDesignConsiderations 10
Sterility-relatedProcessParameters
duringBFSOperations
15
MachineParameterTestSheet
Example
17
ExamplesofContamination
RiskTypesRelatedtoOperation 25
Equipment-relatedSourcesof
Contamination 26
Table
Table
Table
Table
Table
Table
Table
Table
9.0-1
9.0-2
9.0-3
9.0-4
9.0-5
9.0-6
9.0-7
10.0-1
SeverityScoringCriteria 28
ProbabilityofOccurrenceScoring
Criteria 28
LikelihoodofDetectionScoring
Criteria 28
RiskDecisionMatrix 28
RiskPriorityMatrix1-Severity×
Occurrence 29
RiskPriorityMatrix2-Severity×
Occurrence×Detection 29
QualityRiskAssessmentReport
Example 30
AirClassificationsandPrescribed
EnvironmentalParticleLevels 32
1.0Introduction
Blow-Fill-Seal(BFS)technologyistheintegrationofplasticblowmoldingandasepticfillingonasingle
machine.Thetechnologyhasbeenusedinmanufacturingliquidpharmaceuticalproductsincethe1960s.
Thefinalcontaineriscreatedwithinthemachinejustpriortoasepticfillingandhermeticallysealedimme-
diatelyafterfillinginonecontinuous,automatedoperation.ItprovidesauniquecombinationofHexibility
inpackagingdesignandenhancedsteriliryassuranceandhasbeenacceptedworldwideforbothasepticand
terminallysterilizedliquidproducts.BFStechnologyiscurrentlyusedinmorethan50countries(1-4).
Considered“advancedasepticprocessing,”BFStechnologyprovidesadvantagesoverconventionalfilling
whendesigningcontrolsfortheprocesses.Theadvancedasepticprocessingdesignationissupportedby
variousexperimentsthatchallengedBFSsystemsthroughcontaminationloadingofboththesurrounding
environmentandplasticcomponents(5).
BFSprocessingoffersanumberofotheradvantagesaswell.Itsupportsasimplifiedsupplychain,whichcan
resultinalevelofqualityandcontrolofprimarypackagingmaterials(i.e.,resinonly)thatisnotpractical
inpre-formed(glass,plastic,etc.)vial/stopperfilling.Andduetotherapidcool-downfollowingcontainer
formation,biologicalandprotein-basedproductscanbesafelyprocessedinBFSmachines.Theequipment
supportssingle-dosecontainerpackagingwithflexibilityforfrequentchangeoverifshortproductionrunsare
desired.BFSprocessingisalsocapableofincorporatingpre-moldedandpre-sterilizedcomponents(inserts)
inthebasiccontainer,suchassiliconestoppersforparenteralapplicationsandinjection-moldedtip/capin-
sertsformetereddropcontrolinmulti-doseeyedropcontainers.
1.1Purpose
TheobjectiveofthistechnicalreportistoproviderecommendationsspecifictotheoperationofBFStechnol-
ogyforthemanufactureofsterilepharmaceuticals(e.g.,ophthalmic,parenteral,andinhalation).Theintent
istoprovidesupplementalinformationtoassisttheuserwithinterpretationofinternationalstandardsand
regulatoryguidancefromtheperspectiveofBFSoperations.ConsiderationisgiventospecificaspectsofBFS
operationsnotcoveredinpublishedinformation.
1.2Scope
ThistechnicalreportaddressesconsiderationsforBFStechnologyrelatedtotheinstallationandoperation
ofthemachineryandevaluationofrelatedmaterialsandfinalproductcontainers.Supportareas,suchas
laboratory,solutioncompounding,gowningairlocks,etc.,arenotconsideredspecifictoBFSandarenotin-
cludedwithinthescopeofthisdocument.Thistechnicalreportisintendedasaguideforthepharmaceutical
industryandisnotmeanttosupplantorduplicateanyexistingregulatoryguidance.Thecontentandviews
expressedinthistechnicalreportaretheresultofaconsensusachievedbythemembersoftheauthorizing
TaskForceandarenotnecessarilytheviewsoftheorganizationstheyrepresent.
1.3BFSProcessOutline
BFStechnologyisapharmaceuticalprimarypackaging-fillingprocessthatcombinesthreeoperations(con-
tainerformation,filling,andclosure)thataretypicallyperformedseparatelyinconventionalfillingoperations.
BFScontainersareformedfromanextrudedthermoplasticparison,filledwithproduct,andthenscaledin
acontinuous,integrated,highlyautomatedoperation.Originallydevelopedforuseinotherindustries,BFS
technologyhasbeenadaptedforuseinthemanufactureofsterilepharmaceutical,medicaldevice,biological,
andveterinaryproducts.ThetwomostcommontypesofBFSmachinesaretheshurtlingmachine(openor
cutparison)andtherotarymachine(closedparison),whicharebothconsideredinthisdocument.Allsteps
oftheBFSprocessareconductedunderhighlyclassifiedconditionspercurrentregulatorystandards(1,2).
InBFSprocesses,athermoplasticpolymerisusedtoformtheprimarycontainer.Granulatedpolymer(plas-
ticpellets)issuppliedbyaclosedpathwayviavacuumtransfer.Thesystemfeedspolymerpelletsintoa
standardplastichotmeltextrusionprocess.Intheextrusionprocess,thepolymerisheatedtotemperatures
inexcessof170°Candsubjcctedtopressuresover20,000kPa(200bar).
Thetemperature,pressure,andencapsulationwithintheplasticintheextruderreducetheprobabilitythatanycontaminants(suchasparticulates,fungalandbacterialendospores,andendotoxins)maycomeincon-tactwiththefinalfilledproduct(6).
Theplasticpolymerisextrudedintooneormorecontinuousplastictubescalledparisons.Sterilefilteredairorothergasesaresuppliedthroughtheextruderheadatsufficientpressuretopreventtheparisonsfromcollapsing.TheBFSprocessusesoneofrwomechanicalmethodstoformthecontainer(s):1)vacuumonthemoldonly;or2)ablowingprocessincombinationwithvacuumonthemold.Vacuumisemployedwithbothmethodstoremoveairaroundthecontainertoaidincontainerformation.Containerslargerthan30mLtypicallyrequiretheadditionofblowingwithsterileairtocompletethecontainerformation.
Duringoperations,theliquidformulationissuppliedtotheBFSsystemthroughaclosed,sterileproductpathway.TheproductpathwayinBFSisaninherentlysafedesign.Itiscompletelyclosedandallproduct-contactsurfaces,includingthetank,hoses,filterhousings,fillsystem,andfilters(ifprovided,basedonprod-uctspecifications)aretypicallycleanedandsterilizedinplacebeforeproductionbegins.
Themostcommondosingmechanismistimepressuredosing(TPD).Otheracceptabledosingsystemsincludepumpsandpositivedisplacementsystems.Uponcompletionofthedosingstep,thetopportionofthemoldeithercloses(shuttlestyle)orrotatesintocompression(rotarystyle)tosealthecontainer(s)andcompletetheBFSprocess.
TherangeofproductsthatcanbefilledusingBFStechnologyincludessolutions,emulsions,suspensions,andlowandhighviscosityproducts,suchasgels,creams,andointments.
Typicalsolutionscanbeprocessedwithintegratedsterilefiltration.Suspensions,emulsions,andhighlyvis-cousproductscanbeprocessedwithrecirculationandwithoutterminalfiltrationwhereabulksterilizationprocessisimplemented.Inaddition,BFScontainerscanbeterminallysterilizedbysteamandothermethodswhenrequired.Certainlargemoleculeproductscannotbesterilefilteredorterminallysterilized,however,thusaseptictransferoftheproducttotheBFSmachineisrequired.
BFSmachineoutput(containersperhour)isdependentuponproductandpolymerphysicalcharacteristics,andcontainerdesign.Thenumberofcontainersproducedpercycleisonlylimitedbythenumberofcontain-ersthatcanbeformedbythemold.Thecycletimeisdependentupontheproductfllingcharacteristics(c.g,viscosity,foaming)andtheresin-dependentformationtimerequiredinmold.
TechnicalReportNo.77◎2017ParenteralDrugAssociation,Inc.◎2017ParenteralDrugAssociation,Inc.TechnicalReportNo.77
2.0GlossaryofTerms
AdvancedAsepticProcess
Aprocessinwhichdirectinterventionwithopenproductcontainersorexposedproductcontactsur-facesbyoperatorswearingconventionalcleanroomgarmentsisnotrequiredandneverpermitted(3).
AirShower
AdevicefittedtoaBFSmachinewhichprovides,ataminimum,acontinuousHowofGradeAqualityairsupplyoverthefillingneedlesandthepoint-of-fill.Theairshowerisalsoknownasanozzleshroudinshuttletypemachines.
CriticalProcessingZone
Thelocationwithintheasepticprocessingareainwhichproductandproductcontactsurfacesareex-posedtotheenvironment.TheCriticalProcessingZoneisdependentuponmachinedesignandin-cludes,butisnotnecessarilylimitedto,theparisonextrusionandcuttingarea,moldtransferarea,airshower,andpoint-of-fill.
2.1Abbreviations
BFSBlow-Fill-Seal
CIPClean-in-place
CClContainerclosureintegrity
EtOHEthylAlcohol
HDPEHighdensitypolyethylene
LDPELowdensitypolyethylene
Dynamic(inoperation)
BFSmachinelinefullyoperationalandfilling,withthenumberofallowedoperatingpersonnelpresentasduringnormalrunningconditions.
Mandrel
SpecializedfillingneedlesoncertainBFSmachineswhichalsoacttoformthecontainer.
Parison
The"tube"ofpolymerextrudedbytheBFSmachinefromwhichthecontainersareformed.
Static(atrest)
BFSmachinelinewithconveyorbeltsatrestbutwithairshowerandroomventilationinoperation,extruder(heated,notrunning)andmoldcarriageinstandby.Nooperatingpersonnelpresent(1,2).
ZoneofProtection/MachineShroud
AsystemfittedtoaBFSmachinetodirectaHowofHEPA-filteredairovertheCriticalProcessingZoneofthemachine.
LVP
PP
QbD
SIP
SVP
WFI
Largevolumeparenteral
Polypropylene
QualitybyDesign
Sterilization-in-place
Smallvolumeparenteral
Water-for-Injection
3.0BFSEquipment
ForbothshuttleandrotarytypeBFSmachines,thefillingmandrelsaretypicallycleanedpriortousewitha
clean-in-place(CIP)processfollowedbysterilization-in-place(SIP).Thefillingenvironmentismaintained
underGradeAconditionswithHEPA-orsterile-filteredoverpressureair(2).
3.1ShuttleTypeMachines(OpenParisonProcess)
Inanopenparisonprocess,aparisoniscontinuouslyformedthroughtheplasticextrusionprocess.Adown-
wardflowofsterilefilteredair(parisonsupportair)ispassedthroughtheparisontopreventthemolten
plastictubefromcollapsing.Othergases(e.g.,inertgases)canbesubstitutedfortheprocessairduringthe
BFSprocess.Thetwohalvesofamoldclosearoundtheparisontoformthebodyofthecontainer.Simul-
taneously,thenewlyformedcontainerinthemoldiscutfreefromtheparisonbya“knife.”Vacuumisthen
appliedtothemoldtobegincontainerformationandcontinuesuntilformationiscompleted.Figure3.1-1
illustratesanopenparisonBFSprocess.
Step1Parisonpositioning
Step2FilingmandreVnozleinsertion
andcontainerformation
Step3Containerfillingwithproduct
Step4Sealing
Step5Containerrelease
Figure3.1-1DiagrammaticRepresentationoftheOpenParisonBFSProcess
Onceformed,themoldisrapidlytransferred(shuttled)ashortdistancefrombeneaththeparisonheadintothefillingposition(Figure3.1-1,Step1).Thistransfertypicallytakeslessthanonesecond.Thefill-ingmandrel(fillingnozzle)isloweredintotheplastictube.Atthispoint,sterilefilteredairissuppliedtocompletecontainerformation,ifnecessary(blowingstep;Figure3.1-1,Step2).Subsequently,thecontainerisfilledwithameteredvolumeoftheproduct(Figure3.1-1,Step3).Duringtheliquidfil,headspacegasisdisplacedfromwithinthecontainer,eitherthroughthemandrelordirectlytotheambientatmosphere,dependingoncontainerconfiguration.Thefillingmandrelisthenraisedandtheuppersectionofthemold(head/sealmold)isclosed,hermeticallysealingandautomaticallyformingthestill-hotplasticabovethemainmold(Figure3.1-1,Step4).Theentiremoldassemblythenopens,releasingtheformed,filled,andsealedcontainer(Figure3.1-1,Step5).
Containerscanbedischargedfromthemachineassinglecontainers,"packs"ofseveralcontainers,orstripsofmultiplecontainers,dependingonproductrequirements.Afterdischarge,containersaremechanicallydefashed(i.e.,plasticwasteremoved)andseparared.Deflashingtypicallyoccursdirectlyafterdischargeofthecontainer.Thedefashingunitcanbeplacedinthecleanroom,directlyconnectedtothemold,orplacedoutsidethecleanroominthepackagingarea,justdownstreamoftheBFSfillingprocess,tominimizethepotentialforparticulategenerationinthecleanroom.Thismaydependontheresintypeusedandcontainerdesign.Defashingcanbedoneinthecleanroom,ifdesired,becausethecontainerisalreadyclosed.BFSisacontinuousprocesswithonecompletecycletypicallycompletedwithin10-20seconds,dependingoncontainerdesignandfill-volume.
3.2RotaryFillingMachines(ClosedParisonProcess)
BFStechnologycanalsobeappliedtoanoperationusingarotarysysteminwhichthecontainersareformedusingaclosedparisonprocess.Theforming,filling,andsealingofthecontainersintheclosedparisonprocessisidenticaltotheopenparisonprocess,exceptthatthereisnoparisoncuttingbetweeneachBFScycle.Rath-er,thecontainersemergeinacontinuousribbonandareseparatedafterbeingdischargedfromthemachine.Intheclosedparisonprocess,thepossibilityofenvironmentalcontaminationismarkedlyreduced.Eachmoldsetonthechainclosesontheparison,sealingthepreviouscontainerandforminganewcontainer.
RotaryBFSmachinesusemultiplematchedmoldsetsaffixedtotwochainsthatmoveincontinuousmir-rored,counter-rotatingloops.Withrotarytechnology,thefillingmandrelspassdirectlythroughtheextruderhead,asillustratedinFigure3.2.1.Duringcleaningandsterilization,thefillingmandrelsareretractedbackintotheextruderhead.
TechnicalReportNo.77◎2017ParenteralDrugAssociation,Inc.@2017ParenteralDnugAssociation,Inc.TechnicalReportNo.77
Figure3.2-1RotaryBFSMachineSchematic
Theextruderformsacontinuoussingleovalparisonwhichisfedintotherotatingmoldmechanism.Themolds
andchainmoveatthesamespeedastheextrudedplasticparison.Sterileflteredairorothergasunderpositive
presureispassedintotheparisontopreventitfromcollapsing.Asthemoldsetsrotate,theyclosearoundthe
parisontubetoformnewcontainerbodiesandsealofftheprecedingsetofmoldedcontainers.Thecontainersare
formedwithinthemoldthroughvacuumonly.ThisprocessisillustratedinFigure3.2-2.
Toprotecttheproductfromtheheatpresentintheextruderhead,eachfillingmandrelisenclosedwithin
adouble-walledcoolingjacket.Inproduction,thefillingisperformedimmediatelyafterthecontaineris
formed.Duringliquidfilling,theheadspacegaswithinthecontainerisdisplacedbackintotheenclosed
parisonarea.Thecontainersarethendischargedfromthemachineinacontinuousstriporribbon.Typically,
theribbonofcontainersisthenmechanicallydeflashedandseparatedoutsidethefillingroom,accordingto
sterileprocessingguidance(2).Asinglemoldingandfillingcycle(step)takesapproximatelythreetofour
secondstocomplete.
3.3AdditionalApplications
OpenparisonBFSmachinedesignscanaccommodateinsertionofsecondarycomponents,suchasneedles,
rubberstoppers,andcontrolled-dropinserts,beforethecontainerissealed.Anysuchcomponentsshouldbe
sterilizedusingavalidatedprocesspriortoaseptictransferintotheBFSmachinethroughadecontaminated
isolator.Bagscontainingthesterilesecondarycomponentsneedtobedecontaminatedusingaqualifiedpro-
cessastheyaretransferredintotheisolator.
Avariationoftheshuttletypemachinepartitionsthefillingstepfromthesurroundingenvironment;blow-
ingandfillingactivitiestakeplaceattwoseparatestations.Thismachinevariationhasmultiplemoldsrotat-
ingonahorizontalplane.
SealingFilling
Figure3.2-2BFSProcessDetailforRotaryMachines
SomeBFSmachinesalsohaveco-extrusioncapability,whichenablesproductionofamulti-layercontainertoprovideparticularbarrierpropertiesaccordingtotheapplication(c.g.,tominimizevaporlossorpreventgasingress).
Areciprocatingsingle-moldvariation,basedontheclosedparisonrotarytechnology,alsoexists.Reciprocat-ingBFSmachinesuseasingle,verticallyreciprocating,matchedmoldsettoproduceacontinuousribbonoffinishedproduct.
Additionally,BFSmachinescanbeadaptedtoaccommodateheat-sensitiveproducts(e.g.,proteins,vaccines,biologics,andotherlargemolecules).Processvariablescanbemodifiedtoensurethatthereisnodegradationoftheproduct,suchasmodifyingthechilledwaterloopandcontrollingtheproducttemperature(chilling)priortoandafterfilling.Machineparameterscanalsobeadjusted,includingmodificationoffillsystems,toprovideadditionalcooling.
4.0Benefits&SpecialConsiderationsofBFSTechnology
ProperlydesignedandcontrolledBFStechnologyoperationscanofferadvantagesoverconventionalasepticprocessingandfillingoperations,asoutlinedinScction4.1.However,implementationofBFSoperationsrequiresacomprehensiveassessmentandunderstandingoftheprocesstoensuremanufacturingcompatibilitywithBFStechnology.TheseconsiderationsarepresentedinSection4.2.
TechnicalReportNo.77◎2017ParenteralDrugAssociation,Inc.◎2017ParenteralDrugAssociation,Inc.TechnicalReportNo.77
4.1Benefits
1.Durationofexposedproductandcontainer:IntheBFSprocess,thefinalcontainerisformedimmedi-
atelypriortofilling,filled,andsealedinacontinuousoperation,typicallyexposingtheopencontainer
forarelativelyshortdurationoflessthan10seconds.Theresultingbenefitmaybeariskreductionfor
viablemicrobialandforeignparticlecontaminationofproduct.
2.Containerprocessing:Theriskofforeignparticlegenerationduringproduction,processing,packag-
ing,andstorage/transportofglassvialsandrubberstoppersarereducedduetothedirectnatureofBFS
technologycontainerformationandsealingprocess.Inaddition,sincethefinalcontainerisformedjust
priortofilling,proceduresforlineclearancearesimplified.
3.Levelofautomation:BFSmachinesarehighlyautomated,reducingthenumberofoperationsandper-
sonnelrequired.Thereductionofpersonneandinterventionsreducesthepotentialforhumanerrorand
contaminationrisksresultingfromhumanintervention.
4.Machinerydesign:BFSmachinescanbedesignedwithairmanagementconfgurations(e.g.,critical
fill-zoneareashroudedunderacontinuousfowofpositive-pressure,sterilefilteredair),thusminimizing
theimpactandrisksposedbyhumanintervention.Afteranycriticalintervention,theproductpathway
issteamsterilized-in-placebeforeasepticfillingisresumed.
5.Manufacturingspace:BFSprocessdesignallowsforreducedspacerequirementssincethecriticalfill
zoneresideswithintheBFSmachine.TheBFSprocessdoesnotrequirewashing,depyrogenation,cool-
ing,accumulation,filling,stoppering,orcappingstations.
6.Materialsupplychain:BFSreducesthenumberofsuppliersandlogisticsofmaterialsupply,forprimary
packagingrawmaterials,anditprovidesaddedcontrols.ForBFS,theresinsupplieristheonlyprimary
packagingrawmaterialvendorinthesupplychainforthecontainerformedintheBFSprocess.
4.2SpecialConsiderations
1.Processingtemperature:Containersareformedatelevatedtemperarures.Producttemperaruresensitiv-
ityshouldbeconsideredwhendesigningtheprocess.Processparametersandequipmentmayberequired
tominimizehightemperatureimpacttotheproduct.
2.Containermaterialpermeability:PlasticsusedtoformBFScontainersmaybepermeabletogasor
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