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thefurnaceprocessincoal-firedboilers.ThermalEngineering,55,1,72-77.
ControllingtheFurnaceProcessinCoal-FiredBoilers
Theunstabletrendsthatexistinthemarketoffuelsuppliedtothermalpowerplantsandthesituationsinwhichtheparametersoftheiroperationneedtobechanged(orpreserved),aswellasthetendencytowardtheeconomicalandenvironmentalrequirementsplacedonthembecomingmorestringent,arefactorsthatmaketheproblemofcontrollingthecombustionandheattransferprocessesinfurnacedevicesveryurgent.Thesolutiontothisproblemhastwoaspects.Thefirstinvolvesdevelopmentofacombustiontechnologyand,accordingly,thedesignofafurnacedevicewhennewinstallationsaredesigned.Thesecondinvolvesmodernizationofalreadyexistingequipment.Inbothcases,thetechnicalsolutionsbeingadoptedmustbeproperlysubstantiatedwiththeuseofbothexperimentalandcalculationstudies.
TheexperienceCentralBoiler-TurbineInstituteResearchandProductionAssociation(TsKTI)andZiOspecialistsgainedfromoperationofboilersandexperimentalinvestigationstheycarriedoutonmodelsallowedthemtoproposeseveralnewdesignsofmultifuelandmaneuverable—inotherwords,controllable—furnacedevicesthathadbeenputinoperation
atpowerstationsforseveralyears.Alongwiththis,anapproximatezero-one-dimensional,zonewisecalculationmodelofthefurnaceprocessinboilershadbeendevelopedattheTsKTI,whichallowedTsKTIspecialiststocarryoutengineeringcalculationsofthemainparametersofthisprocessandcalculatestudiesoffurnacesemployingdifferenttechnologiesoffiringandcombustionmodes.
Naturally,furnaceprocessadjustmentmethodslikechangingtheairexcessfactor,stackgasrecirculationfraction,anddistributionoffuelandairamongthetiersofburners,aswellasotheroperationswrittenintheboileroperationalchart,areusedduringboileroperation.However,theeffecttheyhaveontheprocessislimitedinnature.Ontheotherhand,controlofthefurnaceprocessinaboilerimpliesthepossibilityofmakingsubstantialchangesintheconditionsunderwhichthecombustionandheattransferproceedinordertoconsiderablyexpandtherangeofloads,minimizeheatlosses,reducetheextenttowhichthefurnaceiscontaminatedwithslag,decreasetheemissionsofharmfulsubstances,andshifttoanotherfuel.Suchacontrolcanbeobtainedbymakinguseofthefollowingthreemainfactors:
(i)theflowsofoxidizerandgasesbeingsettomoveintheflameinadesiredaerodynamicmanner;
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(ii)themethodusedtosupplyfuelintothefurnaceandtheplaceatwhichitisadmittedthereto;
(iii)thefinenesstowhichthefuelismilled.
Thelattercaseimpliesthataflame-bedmethodisusedalongwiththeflamemethodforcombustingfuel.Thebedcombustionmethodcanbeimplementedinthreedesignversions:
mechanicalgrateswithadensebed,fluidized-bedfurnaces,andspouted-bedfurnaces.
Aswillbeshownbelow,thefirstfactorcanbemadetoworkbysettingupbulkyvorticestransferringlargevolumesofairandcombustionproductsacrossandalongthefurnacedevice.Iffuelisfiredinaflame,theoptimalmethodoffeedingittothefurnaceistoadmitittothezonesnearthecentersofcirculatingvortices,asituationespeciallytypicalofhighlyintensefurnacedevices.Thecombustionprocessinthesezonesfeaturesalowairexcessfactor(α<
1)andalonglocaltimeforwhichthecomponentsdwellinthem,factorsthathelpmakethecombustionprocessmorestableandreducetheemissionofnitrogenoxides.
Alsoimportantforthecontrolofafurnaceprocesswhensolidfuelisfiredisthefinenesstowhichitismilled;
ifwewishtominimizeincompletecombustion,thedegreetowhichfuelismilledshouldbeharmonizedwiththelocationatwhichthefuelisadmittedintothefurnaceandthemethodforsupplyingitthere,fortheoccurrenceofunburnedcarbonmaybeduenotonlytoincompletecombustionoflarge-sizefuelfractions,butalsoduetofineonesfailingtoignite(especiallywhenthecontentofvolatilesVdaf<
20%).
Owingtothepossibilityofpictoriallydemonstratingthemotionofflows,furnaceaerodynamicsisattractingagreatdealofattentionofresearchersanddesignerswhodevelopandimprovefurnacedevices.Atthesametime,furnaceaerodynamicsliesattheheartofmixing(masstransfer),aprocessthequantitativeparametersofwhichcanbeestimatedonlyindirectlyorbyspecialmeasurements.Thequalitywithwhichcomponentsaremixedinthefurnacechamberproperdependsonthenumber,layout,andmomentaofthejetsflowingoutfromindividualburnersornozzles,aswellasontheirinteractionwiththeflowoffluegases,withoneanother,orwiththewall.
Itwassuggestedthatthegas-jetthrowdistancebeusedasaparameterdeterminingthedegreetowhichfuelismixedwithairinthegasburnerchannel.Suchanapproachtoestimatinghowefficientthemixingismaytoacertaindegreebeusedinanalyzingthefurnaceasamixingapparatus.Obviously,thegreaterthejetlength(anditsmomentum),thelongerthetimeduringwhichthevelocitygradientitcreatesinthefurnacewillpersistthere,aparameterthatdetermineshowcompletelytheflowsaremixedinit.Notethatthehigherthedegreetowhichajetisturbulizedattheoutletfromanozzleorburner,theshorterthedistancewhichitcovers,and,accordingly,thelesscompletelythecomponentsaremixedin
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thefurnacevolume.Oncethroughburnershaveadvantagesoverswirlonesinthisrespect.
Itiswasproposedthattheextenttowhichoncethroughjetsaremixedastheypenetratewithvelocityw2anddensityρ2intoatransverse(drift)flowmovingwithvelocityw1andhavingdensityρ1becorrelatedwiththerelativejetthrowdistanceinthefollowingway
Whereksisaproportionalityfactorthatdependsonthe―pitch‖betweenthejetaxes(ks=
1.5–1.8).
Theresultsofanexperimentalinvestigationinwhichthemixingofgaswithairinaburnerandtheninafurnacewasstudiedusingtheincompletenessofmixingasaparameterarereportedin5.
Aroundoncethroughjetisintensivelymixedwiththesurroundingmediuminafurnacewithinitsinitialsection,wheretheflowvelocityatthejetaxisisstillequaltothevelocityw2atthenozzleorificeofradiusr0.Thevelocityofthejetblownintothefurnacedropsveryrapidlybeyondtheconfinesoftheinitialsection,andtheaxisithasinthecaseofwall-mountedburnersbendstowardtheoutletfromthefurnace.
OnemayconsiderthattherearethreetheoreticalmodelsforanalyzingthemixingofjetswithflowrateG2thatenterintoastreamwithflowrateG1.Thefirstmodelisforthecasewhenjetsflowintoa―free‖space(G1=0),thesecondmodelisforthecasewhenjetsflowintoatransverse(drift)currentwithflowrateG1G2,andthethirdmodelisforthecase,
whenjetsflowintoadriftstreamwithflowrateG1<
G2.Thesecondmodelrepresentsmixinginthechannelofagasburner,andthethirdmodelrepresentsmixinginafurnacechamber.Weassumethatthemixingpatternwehaveinafurnaceisclosertothefirstmodelthanitistothesecondone,since0<
G1/G2<
1,andwewillassumethatthethrowdistancehofthejetbeingdriftedisequaltothelengthS0ofthe―free‖jet’sinitialsection.Theejectionabilityofthejetbeingdriftedthenremainsthesameasthatofthe―free‖jet,andthelengthoftheinitial
sectioncanbedeterminedusingthewell-knownempiricalformulaofG.N.Abramovich[6]:
S0=0.67r0/a,
(2)whereaisthejetstructurefactorandr0isthenozzleradius.
Ata=0.07,thelengthoftheroundjet’sinitialsectionisequalto10r0andtheradiusthejethasatthetransitionsection(attheendoftheinitialsection)isequalto3.3r0.Themassflowrateinthejetisdoubledinthiscase.Thecorrespondingminimumfurnacecross-sectionalareaFfforaroundoncethroughburnerwiththeoutletcross-sectionalareaFbwillthenbeequaltoandtheratioFf/Fb?
20.Thisvalueisclosetotheactualvaluesfoundinfurnaces
equippedwithoncethroughburners.Infurnacesequippedwithswirlburners,a=0.14andFf/Fb?
10.Inbothcases,theintervalbetweentheburnersisequaltothejetdiameterinthetransitionsectiondtr,whichdifferslittlefromthevaluethathasbeenestablishedinpracticeandrecommendedin[7].
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Themethodtraditionallyusedtocontrolthefurnaceprocessinlargeboilersconsistsofequippingthemwithalargenumberofburnersarrangedinseveraltiers.Obviously,ifthedistancebetweenthetiersisrelativelysmall,operationsondisconnectingorconnectingthemaffecttheentireprocessonlyslightly.Afurnacedesignemployinglargeflat-flameburnersequippedwithmeansforcontrollingtheflamecorepositionusingtheaerodynamicprincipleisastepforward.AdditionalpossibilitiesforcontrollingtheprocessinTPE-214andTPE-215boilerswithasteamoutputof670t/hwereobtainedthroughtheuseofflat-flameburnersarrangedintwotierswithalargedistancebetweenthetiers;
thismadeitpossiblenotonlytoraiseorlowertheflame,butalsotoconcentrateordispersethereleaseofheatinit[1].Averytangibleeffectwasobtainedfrominstallingmultifuel(operatingoncoalandopen-hearth,coke,andnaturalgases)flat-flameburnersintheboilersofcogenerationstationsatmetallurgicalplantsinUkraineandRussia.
Unfortunately,wehavetostatethat,evenatpresent,thoseinchargeofselectingthetype,quantity,andlayoutofburnersinafurnaces