2024年4月11日发(作者:win7清除开机密码)
JournalofHazardousMaterialsA94(2002)1–36
Risk-basedprocesssafetyassessmentandcontrol
measuresdesignforoffshoreprocessfacilities
∗
,RehanSadiq,TahirHusain
FacultyofEngineering&AppliedScience,MemorialUniversityofNewfoundland,
’s,NF,CanadaA1B3X5
Received24August2001;receivedinrevisedform18December2001;accepted20December2001
Abstract
Processoperationisthemosthazardousactivitynexttothetransportationanddrillingoperation
onanoffshoreoilandgas(OOG)periencesofonshoreandoffshoreoilandgas
activitieshaverevealedthatasmallmis-happeningintheprocessoperationmightescalatetoa
ofespecialconcernintheOOGplatformduetothelimitedspaceandcompact
geometryoftheprocessarea,lessventilation,anddiffiGplatform,
eachextracontrolmeasure,whichisimplemented,notonlyoccupiesspaceontheplatformand
increasescongestionbutalsoaddsextraloadtotheplatform.
EventualitiesintheOOGplatformprocessoperationcanbeavoidedthroughincorporatingthe
paper,theauthorsdescribeamethod-
hodologyisapplied
tovariousoffshoreprocessunits,thatis,thecompressor,separators,flashdrumanddriersofan
ntheriskpotential,appropriatesafetymeasuresaredesignedforeachunit.
Thispaperalsoillustratesthatimplementationofthedesignedsafetymeasuresreducesthehigh
Fatalaccidentrate(FAR)valuestoanacceptablelevel.
©htsreserved.
Keywords:Offshoresafety;Offshoreriskassessment;Accidents;Risk-baseddesign;Safetymeasuresdesign
uction
Anoffshoreproductionfacilityinvolvesdrillingrig,structure,transportation,process
plant,worker’cessplantofafullymanned
productionfacilitytypicallyinvolvesanumberofstagesofoil,gasandwaterseparation,
gascompression,kpresentonatypicaloffshoreinstallationmaybe
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E-mailaddress:fkhan@().
0304-3894/02/$–seefrontmatter©htsreserved.
PII:S0304-3894(02)00004-3
∗
al./JournalofHazardousMaterialsA94(2002)1–36
Nomenclature
AP
F1–F3
G
H
c
K
M
NF,NR,NH
pn
pnr
PP
SP
T
TP
V
VP
atmosphericpressure(kPa)
coreenergyfactorsusedindamageindexestimation
coretoxicloadfactorusedintoxicdamageindexestimation
heatofcombustion(kJ/kg)
constant(3148)
massofchemical(kg)ormassreleaserate(kg/s)
NFPArankingforflammability,reactivityandhumanhealth
penaltiesfordamageindexestimation
penaltiesfortoxicdamageindexestimation
processingpressure(kPa)
specificheatratio
temperature(
◦
C)
transportationpressure(kPa)
volumeofchemical(m
3
)
vaporpressure(kPa)
categorizedas:processrisk,droppedobjectrisk,structuralfailurerisk,helicopteraccident
risk,hese,processrisk(riskduetofireandexplosioninthe
processfacility)contributesmorethan50%ofthetotalriskoftheinstallation[1].
Withalloftheavailableoptions,thenumbersofdesignpermutationsareconsiderable.
Anoffshoredevelopmentcanneverbecompletelysafebutthedegreeofinherentsafetycan
beincreasedbyselectingtheoptimumdesignintermsoftheinstallation/fieldconfiguration
andthelayout,whichreducestherisktoalevelthatisaslowasreasonablypracticable
(ALARP)quirestheidentificationof
majorriskcontributorsandtheirassessmentbyusingquantitativeriskassessment(QRA)
techniquesearlyintheprojectlifecycle[2].Ifthestructuredapproachofidentificationand
assessmentisnotcarriedoutearlyintheproject,itispossiblethattheengineeringjudgment
approachwillfailtoidentifyallofthemajorrisksandlosspreventionexpenditurewillbe
targetedinareaswherethereislittlebenefiuldresultedinexpensiveremedial
actionslaterduringthelifeoftheproject.
Giventhenumberofpotentialdesignoptions,itwouldnotbepossible,duetotimeand
resourceconstraints,todevelopalloptionstothepointwhereadetailedQRAstudycould
rlyphaseoftheproject,designoftenchangesasaresultofeconomic
driversorotherexternalinfluences.
CrawleyandGrant[3]
toolpermitstheriskassessmentofmanydesignoptionsinamethodical,consistentand
medatreducingfront-enddesigncostsandtargetingdesignefforts
inacost-effectiveandsafety-orientedmanner.
ThetimeandeffortrequiredtocompleteafullQRAofanoffshoreinstallationisafunction
ofthecomplexityandsizeoftheinstallationwhichintheextremecasecouldrequiremany
monthseffortsspreadoveraprolongedperiod[3,4].Thistimescaleprecludesthesupportof
therapidlychangingdesign,
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