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Publié par | universitat_duisburg-essen |
Publié le | 01 janvier 2010 |
Nombre de lectures | 45 |
Langue | English |
Poids de l'ouvrage | 17 Mo |
Extrait
ExperimentalinvestigationandCFD
simulationoforganicperoxidepoolfires
(TBPBandTBPEH)
VonderFakult¨atf¨urIngenieurwissenschaften,AbteilungMaschinenbauund
Verfahrenstechnikder
Universit¨atDuisburg-Essen
zurErlangungdesakademischenGrades
einesDoktorsderIngenieurwissenschaften
-Ing..Dr
tionDissertaegenehmigt
vno
M.Tech.KirtiBhushanMishra
Indienk,Cuttacaus
Gutachter:Univ.-Prof.Dr.rer.nat.ChristofSchulz
:Univ.-Prof.Dr.rer.nat.AxelSch¨onbucher
Vorsitzender:Univ.-Prof.Dr.-Ing.JohannesWortberg
Tagderm¨undlichenPr¨ufung:12.Mai2010
Acknowledgements
ThisPhDthesishasbeencarriedoutinthecontextofadoctoralprogrammeduringmy
workasaresearchassistantintheworkinggroupon“ExplosiveSubstancesofChemical
Industries”,attheBAMFederalInstituteforMaterialsResearchandTesting.
IexpressmydeepsenseofgratitudetoProf.Dr.rer.nat.AxelSch¨onbucher,De-
partmentofChemicalEngineeringI,UniversityofDuisburg-Essen,campusEssen,for
enablingthisopportunitytoworkunderhiskindsupervision.Iamverythankfulfor
hiscontinuoustechnicalguidanceandscientificdiscussions.Averysincerethankand
deepappreciationtoProf.Dr.rer.nat.ChristofSchulz,InstituteforCombustionand
GasDynamics,DepartmentofMechanicalEngineering,UniversityofDuisburg-Essen
forhisexpertsuggestionsandcommentsondifferenttopicsofinterest.
IwouldliketothankespeciallyProf.Dr.rer.nat.Klaus-DieterWehrstedt,Headof
theDivisionII.2“ReactiveSubstancesandSystems”atBAM.Iamverygratefulfor
hisexpertsuggestions,numerousdiscussionsonvarioustopicsandhispurposefulway
ofworkingwhichalwaysmotivatedandsupportedme.
IwouldalsoliketothankDr.rer.nat.HeikeMichael-Schulz,HeadoftheWork-
ingGroupII.23“ExplosiveSubstancesofChemicalIndustries”atBAMforproviding
excellentsupportandco-operationforconductingtheexperiments.
Also,IwishtothankDr.-Ing.MichaelRudolphandDr.rer.nat.MarcusMalowfrom
BAMII.2andDr.-Ing.AnjaHofmannandDr.rer.nat.SimoneKru¨gerfromBAM
VII.3forthefruitfuldiscussionsandtechnicalknowhows,particularlyforexperimental
work.MyspecialthankstoallcolleaguesDipl.-Ing.GerhardReinhardZemke,Dipl.-
Ing.JochenKebben,Dipl.-Ing.KimStattaus,Mr.Klaus-DieterNicolaus,Ms.Bianca
Fourier,Dipl.-Ing.Kai-UweZiener,Dipl.-Ing.MartinBeckmannKlugeandDipl.-Ing.
ReinholdWendlerofBAMforco-operationandgreatassistanceintheimplementation
ofexperimentalstudies.Mr.MichaelBulinisthankfullyacknowledgedforthecluster
administrationofBAMIIforcarryingoutsimulations.IamverythankfultoDr.rer.
nat.IrisVela,Dipl.-Phys.PeterSudhoffandDr.rer.nat.MarkusGawlowskifromthe
InstituteofChemicalEngineeringI,UniversityofDuisburg-Essen,Essencampus,for
theexcellentcooperation,friendlysupportandassistanceincomputationalwork.
Iamalsoverythankfultojoshijiandashwinibhabhiforthearrangementofrefreshing
tea-breaksandthecompaniesofpurvaandmaololanduringthelunchtime.
iii
ShriNarsinghaDevayNamah
Dedicatedtomyparents(ShriNarayanPrasadMishraand
ShrimatiPriyambadaMishra)andmylovingbrothers(ShriVibhuti
BhushanMishra,ShriShashiBhushanMishra,ShriRaviBhushan
MishraandShriChandraBhushanMishra)andtheirfamiliesand
toallmybelovedonesthecompanyofwhomimissedalot..........
v
ABSTRACT
Timeaveragedmassburningrate(m˙f),flamelength(H),temperature(T),irradi-
ance(E)andsurfaceemissivepower(SEP)ofTBPB(tert-butylperoxybenzoate)and
TBPEH(tert-butylperoxy-2-ethylhexanoate)poolfiresaremeasuredforsixpooldi-
ameters(d=0.059m,0.107m,0.18m,0.5m,1mand3.4m)atBAMinhouseand
outsidetestfacility.
Themeasuredheatsofcombustion(–Δhc)ofTBPBandTBPEHare30113kJ/kgand
34455kJ/kgandthespecificheatcapacitiesatconstantpressure(cp)are1.8kJ/(kgK)
and2.1kJ/(kgK)respectively.
Themeasuredm˙fofTBPBandTBPEHpoolfiresareintherangeof0.37kg/(m2s)≤
m˙f≤0.83kg/(m2s)andshowlittledependenceonthepooldiameterd,andarefour
tosixtytimeshigher(ford=1m)thanthatofhydrocarbonpoolfires.Itisshown
thatthemassburningratesoftheinvestigatedorganicperoxidescanberepresented
asanexponentialfunctionoftheself-acceleratingdecompositiontemperature(SADT).
LowSADTimpliesthattheorganicperoxidepoolfiresburnatamuchhigherm˙fthan
hydrocarbonpoolfires.
FuelFroudenumbers(Frf)ofTBPBandTBPEHare5to100times(dependingond)
higherthanforhydrocarbonpoolfires.DuetohigherFrftheHofTBPBandTBPEH
(measuredwithaS-VHSVideocamera)arefoundtobetwotimeslarger(d=1m)than
correspondingpoolfiresofhydrocarbons.Heskestadsflamelengthcorrelationpredicts
thedH(d=3.4m)ofTBPBandTBPEHpoolfiresmuchbetterthanThomasandFay
.scorrelationThemeasuredtimeaveragedflametemperaturesT(d=3.4m)forTBPBandTBPEH
poolfiresareintherangeof1400K≤T≤1500Kandare200Kto300Khigherthan
forJP-4,keroseneandgasoline.
TheirradiancesoftheTBPBandTBPEHpoolfiresmeasuredbyradiometersareE
(Δy/d=0.3)=45kW/m2andE=98kW/m2whicharetwototentimeshigherin
comparisontothecorrespondingn-pentane,supergasolineanddieselpoolfires.Sothe
thermalsafetydistancesfororganicperoxidepoolfiresarelargerbyafactorfourin
comparisontothehydrocarbonpoolfires.
AninfraredthermographysystemisusedforthedeterminationofSEPofTBPBand
TBPEHpoolfires.ThevaluesofsurfaceemissivepowerforTBPBandTBPEHare
SEP(d=3.4m)=196kW/m2andSEP=258kW/m2andthustheSEParebya
factorofapproximatelytwohigherthanforhydrocarbonpoolfires.
Aself-sustainedpulsatingdH(’W’-Effect)isfoundinTBPBpoolflamesandisfurther
analysedtoexplainthereasonofoccuranceonthebasisofchemicalstructureofthefuel
anddiscontinuousheatfluxbackfromflametotheliquidpool.
CFDsimulationsofTBPBandTBPEHpoolfiresatd=0.18m,0.5m,1m,3.4mand8
marecarriedoutusingtheUnsteadyReynoldsAveragedNavierStokes(URANS)equa-
tions.Thethree-dimensionalgeometrieshavebeendiscritizedwithunstructuredhybrid
grids,withthenumberofcellsintherangeof1million.Dependingonthegridresolu-
tionandthepooldiametertimestepsof0.0001s≤Δt≤0.01sfortheCFDsimulations
areused.ForsolvingthediscritizedequationsafinitevolumebasedimplicitsolverAN-
SYSCFXhasbeenused.Formodellingthecombustion,stoichiometriccombustionfor
bothperoxidesareassumed.Thetemperaturedependenceofthereactionratehasbeen
determinedbytheArrheniusapproach.Formodellingthecombustioneddydissipation
concept(EDC)modelhasbeenused.Forturbulencebuoyancymodifiedk-andSAS
(ScaleAdaptiveSimulation)turbulencemodelsareused.Forthethermalradiationand
sootmassfractiondiscretetransferradiationmodelandMagnussonsootmodelhave
beenused.
Anewmethodissuggestedforthepredictionofmassburningrate(m˙f)byCFDsimula-
tion.Bothperoxidepoolfiresshowapproximatelyconstantmassburningrateindepen-
dentofdwhereasm˙fofTBPEHareunderpredictedatthebeginningbutshowrelatively
goodagreementwithmeasurementsforlargepooldiameters(d=1m).IncaseofTBPB
theCFDsimulationoverpredictsthemassburningratem˙fofsmallTBPBpoolfires
andshowsacontinuousdecreasewithd.CFDpredictstheflamelengthHclosetothe
measureddataprovidedthattheconstantsinThomasequationaremodified.
TheCFDpredictedtimeaveragedsurfaceemissionflametemperaturesofTBPBand
TBPEHpoolfires(d=3.4m,1437Kand1542K)areingoodagreementwiththe
measuredtimeaveragedflametemperatures.
TheCFDpredictedSEPforTBPBandTBPEHpoolfires(d=3.4m,217kW/m2and
288kW/m2)arealsoinagreementwiththemeasuredvalues.FromtheCFDpredicted
irradianceECFDitispossibletodeterminethethermalsafetydistancesfromlargepool
firesofhydrocarbonsandorganicperoxides.
Contents
ixiiatureNomenclxvsrLetteGreekxviisIndicexixionsAbbreviatxxianeousMiscell1ductiontroIn12TheoreticalBackground5
2.1Introduction...................................5
2.2Dynamicsofpoolfires.............................5
2.2.1Massburningrate...........................8
2.2.1.1TheoryofburningrateaccordingtoHertzberg......12
2.2.1.2Effectoflipheight,thicknessandpanmaterial......13
2.2.2Flamelength..............................13
2.2.2.1FlamelengthmodelaccordingtoThomas.........16
2.2.2.2FlamelengthmodelaccordingtoSteward.........17
2.2.2.3FlamelengthmodelaccordingtoMcCaffrey.......17
2.2.2.4FlamelengthmodelaccordingtoMoorhouse.......18
2.2.2.5FlamelengthmodelaccordingtoHeskestad........18
2.2.2.6FlamelengthmodelaccordingtoFay...........19
2.2.2.7Effectofunsteadiness....................21
2.2.3Flametemperatureandflowvelocity.................21
2.2.4Adiabaticflametemperature.....................25
2.2.5Thermalradiation...........................25
2.2.5.1Pointsourcemodel.....................25
2.2.5.2Conventionalandmodifiedsolidflameradiationmodel.27
2.2.5.3Viewfactors.........................31
2.2.5.4Atmosphericabsorption...................33
2.2.6OrganisedStructuresRadiationModels(OSRAMOII,OSRAMO
III)....................................33
2.3Organicperoxides...............................34
2.3.1SelfAcceleratingDecompositionTemperatureoforganicperoxides37
2.3.2Fireandexplosionhazardsoforganicperoxides...........38
ix
xtstenCon2.4Modellingandsimulationofpoolfires....................39
3ExperimentalInvestigations41
3.1Descriptionofmeasuringinstruments.....................41
3.1.1DynamicDifferentialCalorimetry(DDC)..............41
3.1.2Thermocouples.............................43
3.1.3Thermographiccamera........................44
3.1.4Radiometers..............................45
3.2Experimentalset-upsforsmallandlargescalefiretests..........46
3.2.1Construction..............................46
3.2.2Fuels...................................47
3.2.3Massburningrate...........................48
3.2.4Flamelength..............................48
3.2.5Flametemperature...........................48
3.2.6Surfaceemissivepower