ch11Flue Gas Desulfurization Systems.docx
- 文档编号:4352736
- 上传时间:2022-11-30
- 格式:DOCX
- 页数:18
- 大小:66.60KB
ch11Flue Gas Desulfurization Systems.docx
《ch11Flue Gas Desulfurization Systems.docx》由会员分享,可在线阅读,更多相关《ch11Flue Gas Desulfurization Systems.docx(18页珍藏版)》请在冰豆网上搜索。
ch11FlueGasDesulfurizationSystems
FlueGasDesulfurizationSystems
TimothyW.DevittP.E.
Vice-President
PEDCoEnvironmental,Inc.
Cincinnati,Ohio
11.1DESCRIPTIONOFCONTROLDEVICE
Fluegasdesulfurization(FGD)istheprocessofremovingsulfuroxides,primarilySO2,fromcombustiongases.InwetprocessFGDsystems,fluegasesarecontactedwithanabsorbentinavesselcalledeitheranabsorberorascrubber.TheSO2reactswiththeabsorbentordissolvesintothesolutiontoproduceaslurryorliquidthatcontainsdissolvedorsolidifiedsulfurcompounds.Inalloperatingsystems,waterisusedtodissolveorsuspendthereactingchemicals,althoughanumberofdryabsorptionsystemsarecurrentlybeingcommercialized.TheadvantagesofdryscrubbingincludepotentialcostandenergysavingsandrelativeeaseofoperationcomparedwithwetFGDsystems.Dryscrubbing,however,requireshigherchemicalconsumptionandmayberestrictedtolow-sulfurcoals.Becausemostofthecommercialdryscrubbinginstallationsareunderconstructionorintheplanningphase,thereisalackofdataonfull-scalesystems.Therefore,thisreviewislimitedtowetFGDsystems.
WetFGDprocessesaregroupedintotwogeneralcategories,regenerableandnonregenerable,dependingonwhetherthesulfurisseparatedfromtheabsorbentaswaste.Nonregenerableprocessesproduceasludgethatrequiresdisposalinanenvironmentallysoundmanner.Regenerableprocessesincludeadditionalstepstoconvertthesulfurintoby-productssuchasliquidsulfurdioxide,sulfuricacid,orelementalsulfur.
SixbasicwetFGDsystemsareusedinthiscountry,primarilytotreatfluegasfromlarge,coal-firedboilers.Ofthese,thelimescrubbing,limestonescrubbing,sodiumcarbonatescrubbing,anddualalkalisystemsareclassifiedasnonregenerable.ThemagnesiumoxidescrubbingandWellman-Lordsystemsareclassifiedasregenerableprocesses.
Table11-1liststhemajorregenerableandnonregenerablesystemsandindicatesthenumberofsystemsthatareoperational,underconstruction,orplannedforapplicationonbothutilityandnonutilityboilers.
BecausemostoperatingFGDsystemsarenonregenerable(atrendthatislikelytocontinuebecauseoftheirgenerallylowercapitalandoperatingcosts),onlytheregenerablesystemsarereviewedhere.Furthermore,onlythewetlime-andlimestone-basedsystemsarediscussed,althoughmanyofthedesign,operation,andmaintenanceconsiderationsaresimilarforothersystems.
TABLE11-1DistributionofFGDsystemsbyprocesstype.
Process
UTILITYBOILERFGDCAPACITY(MW)1.2
Process
INDUSTRIALBOILERFGDCAPACITY(SCFM)3.4
Operational
UnderConstruction
Planned
Total
Operational
UnderConstructionPlanned
Total
Aqueouscarbonate/spraydrying
100
100
Ammonia
164,000
154,000
318,000
Citrate
605
605
Caustic
211,000
211,000
Dualalkali
1,201
842
2,043
Causticwastestream
665,000
665,000
Lime
8,801
2,060
6,841
17,702
Citrate
142,0005
142,0005
Limestone
11,437
7,637
17,254
36,328
Dualalkali
1,480,000
1,480,000
Limestone/alkalineflyash
1,480
1,480
Dualalkali(concentrated)
489,070
512,000
1,001,070
Lime/alkalineflyash
2,613
1,400
4,013
Dualalkali(dilute)
233,400
233,400
Lime/limestone
20
475
495
Lime
40,000
30,000
70,000
Lime/spraydrying
110
1,060
1,813
2,983
Lime/spraydrying
72,700
72,700
Magnesiumoxide
724
724
Limestone
55,000
55,000
Sodiumcarbonate
925
330
1,900
3,155
Sodiumcarbonate
2,467,000
504,500
2,971,500
Sodiumcarbonate/spraydrying
440
440
Sodiumhydroxide
1,140,300
12,000
1,152,300
WellmanLord
1,540
534
2,074
Sulf-xscore
10,000
10,000
Processnotselected
6,650
6,650
Processnotselected
124,000
124,000
Total
28,187
14,285
35,775
78,247
Total
5,464,770
3,041,200
8,505,970
1M.Smith,etal.,EPAUtilityFGDSurvey:
October-December1980.Vol.1.EPA-600/7-81-012a,PEDCoEnvironmental,Cincinnati,Ohio,October1979.2Capacitiesarereportedasequivalentscrubbedcapacity(ESC);thesummationofeffectivescrubbedfluegasinequivalentMWbasedonthepercentofthefluegasscrubbedbytheFGDsystem(s).3J.Tuttle,etal.,EPAIndustrialBoilerFGDSurvey:
FirstQuarter1979.EPA-600/7-79-067b,PEDCoEnvironmental,Cincinnati,Ohio,April1979.4Forapproximatecomparisonpurposes1MWmaybeconsidered≈3000scfm.5ThecitrateprocessFGDsystemonSt.JoeZinc’sG.F.Weatonunitwasincludedinboththeutilityandindustrialreportsinceitsuppliespowertotheutilitygridaswellassteamfortheindustrialplant.Thisunitshouldbedeletedfromoneortheothersectionswhenestimatingtotalprocesscapacitiesfortheindustrial-utilitymarketplaceasawhole.
TheLimeScrubbingProcess
Thefirststepoftheprocessispreparationofalimeslurry.Lime(CaO)isreactedwithwaterinaslaker[]石灰消和器toproduceaslurryofcalciumhydroxide[Ca(OH)2]andwater,accordingtothefollowingreaction:
CaO+H2O→Ca(OH)2+heat.Thismaterialisdiluted[]无力的,冲淡的withrecycledwatertoproduceascrubberslurrycontainingabout15to20%solids.
Thelimeslurryisaddedataregulatedratetoarecycletankthatcontainsthescrubbingslurry.Largepumpscirculatethescrubbingslurrythroughthescrubberorabsorbervessel.Intheabsorber,theslurrydropletsarebroughtintocontactwiththefluegascontainingSO2,andtheSO2passesfromthegasintothedropletsdrivenbyaconcentrationgradient.ThedissolvedSO2reactswithcalciumfromthelimeaccordingtothefollowingreactions:
Ca(OH)2(s)↔Ca(OH)2(aq)↔Ca
+2OH‾
2OH‾+CO2↔CO
+H2O
CO
+CO2+H2O↔2HCO
Ca2++CO
↔CaCO3
CaCO3(s)↔CaCO3(aq)↔Ca2++CO
SO2(g)↔SO2(aq)+H2O↔H++HSO
HSO
↔H++SO
Ca2++SO
↔CaSO3(aq)
Ca2++SO
+1/2H2O↔CaSO3•1/2H2O(s)
CaSO3+H+↔Ca2++HSO
H++HCO
↔H2CO3↔CO2(g)+H2O
CaSO3•1/2H2O+3/2H2O+1/2O2↔CaSO4•2H2O
Thesereactionstakeplacetosomeextentineverytimescrubbingsystem;similarreactionsoccurinlimestonesystems.Suchfactorsasionicconcentrations,pH,temperature,andretentiontimeinthereactiontankinfluencethespeedandcompletenessofthevariousreactions.Theneteffect,however,isremovalofSO2fromthefluegas,depletionofcalciumhydroxideintheslurry,andgenerationofinsolublecalciumsulfiteandcalciumsulfate.Thecalciumionsusedinthereactionsarereplenishedbydissociationofcalciumhydroxide.Theuseofaninsolublealkalinereagentistheprimarydifferencebetweenthelimeandlimestoneslurryscrubbingsystemsandtheso-calledclearsolutionscrubbers(e.g.,doublealkaliscrubbers),wherethepredominantreactivealkali(sodium)ismoresoluble.
Forcingmostofthesulfite/sulfateprecipitationtooccurinthereactiontankrequiresacertainamountofretentiontimetopermittheslurrytoreachchemicalequilibriumbeforeitisrecirculatedtothescrubber.Forthispurpose,areactiontank,sometimesanintegralpartofthescrubbervessel,isusuallysizedwitharetentiontimeofbetween5and10minutes.
Thecalciumsulfiteandcalciumsulfatethatareformedinthereactiontankmustberemovedfromthesystem.Thisisaccomplishedbybleedingastreamfromtherecirculatingslurrytoathickenerorclarifier.Thecalciumsulfiteandsulfatesettleoutandareremovedfromtheunderflowoftheclarifierinaslurryofabout30%solids.Theoverflow,aclearliquidoflessthan1%solids,isbroughtbacktothesystemforreuseintheprocess.Thesludgefromtheunderflowisdisposedofbyoneofseveralmeans.
Onemethodofdisposalistopumpthesludgetoapond.Inthiscasethesludgeispumpedfromthethickenerunderflow(oroccasionallydirectlyfromthereactiontank)toalargepond,wherethesolidssettle.Clearwaterisrecycledfromthepond,asnecessary,tokeepthepondfromoverflowing.Returnofallthisclearliquorfromthepondtotheprocessiscalleda“closed-loop”operation.
Anothermethodofdisposalistodewaterthesludgeinavacuumfilter,chemicallystabilizeitbytheuseofgenericorproprietaryprocesses,anddisposeofitinalandfill[]n.垃圾掩埋法,垃圾.Whenvacuumfiltrationisused,thefiltrateisreturnedtothesystemtocreateclosed-loopoperation.
TheLimestoneScrubbingProcess
Limestoneslurrypreparationistheonlystepthatissignificantlydifferentfromthelimescrubbingprocess.Lumpsizelimestoneispulverized[]v.研磨成粉to-200to–300meshinaballmillandslurriedwithwater.ThefinesizeisneededbecausedissolutionofCaCO3isaslowreaction,theratebeingdirectlyrelatedtotheparticlesurfaceareaandthereforetotheparticlesize.Forfurtherlimestonedissolution,thescrubbingslurryismaintainedatanacidicpH,incontrasttolime-basedsystems,inwhichscrubbingslurryisslightlyalkaline.Theoverallprocessreactionsarethesameasforthelimeslurryscrubbingprocess,exceptthereactantspeciesisCaCO3,notCa(OH)2.
Figure11-1illustratesatypicallimestoneprocess.Thelimeprocessissimilarexceptalimeslakerreplacestheballmillofthelimestoneprocess.
OtherwetprocessFGDsystemsoperatesimilarly.TheSO2isscrubbedfromthegasesinacontactor,andreactionproductsareremovedinaseparatevessel.Severalexcellenttextsandreportsareavailablethatdescribethevarioussystems,theirchemistry,andstatusofcommercialization;thesearelistedinSection11.8.
11.2DESIGNPROCEDURES
Propersystemdesigniscrucial[]极重要的tosuccessfuloperationofanFGDsystem.Althoughthisistrueforallairpollutioncontrolsystems,itisespeciallyimportantforFGDsystems.Incontrasttom
- 配套讲稿:
如PPT文件的首页显示word图标,表示该PPT已包含配套word讲稿。双击word图标可打开word文档。
- 特殊限制:
部分文档作品中含有的国旗、国徽等图片,仅作为作品整体效果示例展示,禁止商用。设计者仅对作品中独创性部分享有著作权。
- 关 键 词:
- ch11Flue Gas Desulfurization Systems
![提示](https://static.bdocx.com/images/bang_tan.gif)