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1、1ControllingtheFurnaceProcessinCoalFiredBoilersTheunstabletrendsthatexistinthemarketoffuelsuppliedtothermalpowerplantsthesituationsinwhichtheparametersoftheiroperationneedtobechanged(preserved)aswellasthetendencytowardth
2、eeconomicalenvironmentalrequirementsplacedonthembecomingmestringentarefactsthatmaketheproblemofcontrollingthecombustionheattransferprocessesinfurnacedevicesveryurgent.Thesolutiontothisproblemhastwoaspects.Thefirstinvolve
3、sdevelopmentofacombustiontechnologyaccdinglythedesignofafurnacedevicewhennewinstallationsaredesigned.Thesecondinvolvesmodernizationofalreadyexistingequipment.Inbothcasesthetechnicalsolutionsbeingadoptedmustbeproperlysubs
4、tantiatedwiththeuseofbothexperimentalcalculationstudies.TheexperienceCentralBoilerTurbineInstituteResearchProductionAssociation(TsKTI)ZiOspecialistsgainedfromoperationofboilersexperimentalinvestigationstheycarriedoutonmo
5、delsallowedthemtoproposeseveralnewdesignsofmultifuelmaneuverable—inotherwdscontrollable—furnacedevicesthathadbeenputinoperationatpowerstationsfseveralyears.Alongwiththisanapproximatezeroonedimensionalzonewisecalculationm
6、odelofthefurnaceprocessinboilershadbeendevelopedattheTsKTIwhichallowedTsKTIspecialiststocarryoutengineeringcalculationsofthemainparametersofthisprocesscalculatestudiesoffurnacesemployingdifferenttechnologiesoffiringcombu
7、stionmodes.Naturallyfurnaceprocessadjustmentmethodslikechangingtheairexcessfactstackgasrecirculationfractiondistributionoffuelairamongthetiersofburnersaswellasotheroperationswrittenintheboileroperationaltareusedduringboi
8、leroperation.Howevertheeffecttheyhaveontheprocessislimitedinnature.Ontheotherhcontrolofthefurnaceprocessinaboilerimpliesthepossibilityofmakingsubstantialchangesintheconditionsunderwhichthecombustionheattransferproceedind
9、ertoconsiderablyexptherangeofloadsminimizeheatlossesreducetheextenttowhichthefurnaceiscontaminatedwithslagdecreasetheemissionsofharmfulsubstancesshifttoanotherfuel.Suchacontrolcanbeobtainedbymakinguseofthefollowingthreem
10、ainfacts:3estimatinghowefficientthemixingismaytoacertaindegreebeusedinanalyzingthefurnaceasamixingapparatus.Obviouslythegreaterthejetlength(itsmomentum)thelongerthetimeduringwhichthevelocitygradientitcreatesinthefurnacew
11、illpersistthereaparameterthatdetermineshowcompletelytheflowsaremixedinit.Notethatthehigherthedegreetowhichajetisturbulizedattheoutletfromanozzleburnertheshterthedistancewhichitcoversaccdinglythelesscompletelythecomponent
12、saremixedinthefurnacevolume.Oncethroughburnershaveadvantagesoverswirlonesinthisrespect.Itiswasproposedthattheextenttowhichoncethroughjetsaremixedastheyperatewithvelocityw2densityρ2intoatransverse(drift)flowmovingwithvelo
13、cityw1havingdensityρ1becrelatedwiththerelativejetthrowdistanceinthefollowingwayWhereksisaproptionalityfactthatdependsonthe“pitch”betweenthejetaxes(ks=1.5–1.8).Theresultsofanexperimentalinvestigationinwhichthemixingofgasw
14、ithairinaburnertheninafurnacewasstudiedusingtheincompletenessofmixingasaparameterarereptedin5.Aroundoncethroughjetisintensivelymixedwiththesurroundingmediuminafurnacewithinitsinitialsectionwheretheflowvelocityatthejetaxi
15、sisstillequaltothevelocityw2atthenozzleificeofradiusr0.Thevelocityofthejetblownintothefurnacesveryrapidlybeyondtheconfinesoftheinitialsectiontheaxisithasinthecaseofwallmountedburnersbendstowardtheoutletfromthefurnace.One
16、mayconsiderthattherearethreetheeticalmodelsfanalyzingthemixingofjetswithflowrateG2thatenterintoastreamwithflowrateG1.Thefirstmodelisfthecasewhenjetsflowintoa“free”space(G1=0)thesecondmodelisfthecasewhenjetsflowintoatrans
17、verse(drift)currentwithflowrateG1G2,thethirdmodelisfthecase?whenjetsflowintoadriftstreamwithflowrateG1G2.Thesecondmodelrepresentsmixinginthechannelofagasburnerthethirdmodelrepresentsmixinginafurnacechamber.Weassumethatth
18、emixingpatternwehaveinafurnaceisclosertothefirstmodelthanitistothesecondonesince0G1G21wewillassumethatthethrowdistancehofthejetbeingdriftedisequaltothelengthS0ofthe“free”jet’sinitialsection.Theejectionabilityofthejetbein
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