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FOSSIL POWER SYSTEMS INC. 1| Page STEAM DRUM WATER LEVEL MEASUREMENT A. Introduction. Boiler steam drum water level is one of the most important power plant parameters to both measure and control. Control of the proper water level in the boiler is critical for safe operation of the boiler. If the level is too low, boiler tubes will be damaged by overheating. If the level is too high, steam separators will not function properly, temperature control will be difficult, and the superheater tubes and turbine could be damaged by moisture or water treatment chemical carryover. In addition, poor level control will also adversely affect the drum pressure control. The sliding operating pressure of modern 3 drum Heat Recovery Steam Generators, along with frequent startup and shut down, has added to the challenge of selecting the proper mix of instruments and maintaining correct water levels under all conditions. Although instruments for drum water level measurement have been around for well over a hundred years, it is important to understand the operating principles, installation requirements, strengths and weaknesses of each technology. To ignore these considerations can lead to misapplication, increased maintenance, poor instrument performance, and unsafe operation. The ASME Boiler and Pressure Vessel Code Section I establishes the requirements for steam drum water level measurement in fired steam drums. The primary focus of these requirements is safe boiler operation. Maintenance, performance, and other specific application issues are not addressed. There are a dozen or more level technologies that could be considered for this application. The purpose of this paper is to review 5 of the proven technologies currently available for high pressure steam drum water level measurement. These will be compared with the current ASME Section 1 requirements (2010 code edition), and also evaluate the installation, performance characteristics, strengths and weaknesses of each. B. ASME Requirements. The ASME Boiler and Pressure Vessel Code Section I paragraph PG60 lists the majority of the requirements for water level measurement instruments. The primary focus is safe and reliable drum level indication at all times. This is an important consideration in order to understand why changes to the code are made slowly and deliberately. Other requirements pertaining to level instruments are listed in PG5 (materials of construction) and PG12 (water level indicators and connector material). The ASME code requirements have continuously evolved over the years. Instrument use, incident reports and performance history are evaluated. In addition, “Interpretations” are published annually to answer questions submitted to the ASME code committee pertaining to various code sections. The results of the most important “Interpretations” are later written into the various code paragraphs to permanently clarify sections that might have been confusing and misapplied. Below are listed the most important code requirements. This is not a complete listing. I will later list and discuss specific requirements and interpretations applicable to particular instrument types.

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  • FOSSILPOWERSYSTEMSINC.

    1|P a g e

    STEAMDRUMWATERLEVELMEASUREMENT

    A. Introduction.Boilersteamdrumwaterlevelisoneofthemostimportantpowerplantparameterstobothmeasureandcontrol.Controloftheproperwaterlevelintheboileriscriticalforsafeoperationoftheboiler.Ifthelevelistoolow,boilertubeswillbedamagedbyoverheating.Ifthelevelistoohigh,steamseparatorswillnotfunctionproperly,temperaturecontrolwillbedifficult,andthesuperheatertubesandturbinecouldbedamagedbymoistureorwatertreatmentchemicalcarryover.Inaddition,poorlevelcontrolwillalsoadverselyaffectthedrumpressurecontrol.Theslidingoperatingpressureofmodern3drumHeatRecoverySteamGenerators,alongwithfrequentstartupandshutdown,hasaddedtothechallengeofselectingthepropermixofinstrumentsandmaintainingcorrectwaterlevelsunderallconditions.Althoughinstrumentsfordrumwaterlevelmeasurementhavebeenaroundforwelloverahundredyears,itisimportanttounderstandtheoperatingprinciples,installationrequirements,strengthsandweaknessesofeachtechnology.Toignoretheseconsiderationscanleadtomisapplication,increasedmaintenance,poorinstrumentperformance,andunsafeoperation.TheASMEBoilerandPressureVesselCodeSectionIestablishestherequirementsforsteamdrumwaterlevelmeasurementinfiredsteamdrums.Theprimaryfocusoftheserequirementsissafeboileroperation.Maintenance,performance,andotherspecificapplicationissuesarenotaddressed.Thereareadozenormoreleveltechnologiesthatcouldbeconsideredforthisapplication.Thepurposeofthispaperistoreview5oftheproventechnologiescurrentlyavailableforhighpressuresteamdrumwaterlevelmeasurement.ThesewillbecomparedwiththecurrentASMESection1requirements(2010codeedition),andalsoevaluatetheinstallation,performancecharacteristics,strengthsandweaknessesofeach.

    B. ASMERequirements.TheASMEBoilerandPressureVesselCodeSectionIparagraphPG60lists

    themajorityoftherequirementsforwaterlevelmeasurementinstruments.Theprimaryfocusissafeandreliabledrumlevelindicationatalltimes.Thisisanimportantconsiderationinordertounderstandwhychangestothecodearemadeslowlyanddeliberately.OtherrequirementspertainingtolevelinstrumentsarelistedinPG5(materialsofconstruction)andPG12(waterlevelindicatorsandconnectormaterial).TheASMEcoderequirementshavecontinuouslyevolvedovertheyears.Instrumentuse,incidentreportsandperformancehistoryareevaluated.Inaddition,InterpretationsarepublishedannuallytoanswerquestionssubmittedtotheASMEcodecommitteepertainingtovariouscodesections.TheresultsofthemostimportantInterpretationsarelaterwrittenintothevariouscodeparagraphstopermanentlyclarifysectionsthatmighthavebeenconfusingandmisapplied.Belowarelistedthemostimportantcoderequirements.Thisisnotacompletelisting.Iwilllaterlistanddiscussspecificrequirementsandinterpretationsapplicabletoparticularinstrumenttypes.

  • FOSSILPOWERSYSTEMSINC.

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    TheprimaryrequirementsinASMEPG60(2009)areasfollows:1. (PG60.1)Allboilershavingafixedwaterlevel(steamandwaterinterface)shallhaveatleast

    onegageglass(atransparentdevicethatpermitsvisualdeterminationofthewaterlevel).2. (PG60.1.1)Boilershavingamaximumallowableworkingpressureexceeding400psi(3MPa)

    shallhavetwogageglasses.Insteadofoneofthetworequiredgageglasses,twoindependentremotewaterlevelindicators(twodiscretesystemsthatcontinuouslymeasure,transmit,anddisplaywaterlevel)maybeprovided.

    3. (PG60.1.1)Whenthewaterlevelinatleastonegaugeglassisnotreadilyvisibletotheoperatorintheareawherecontrolactionsareinitiated,eitherafiberopticcable(withnoelectricalmodificationoftheopticalsignal)ormirrorsshallbeprovidedtotransfertheopticalimageofthewaterleveltothecontrolarea.Alternatively,anycombinationoftwoofthefollowingshallbeprovided:

    a. Anindependentremotewaterlevelindicatorb. Anindependentcontinuoustransmissionanddisplayofanimageofthewaterlevelina

    gageglass.4. (PG60.1.1.2)Whentwoindependentremotewaterlevelindicatorsareinreliableoperation

    (continuouslyindicatingwaterlevel),theonerequiredgageglassmaybeshutoff,butshallbemaintainedintheserviceablecondition.

    INTERPRETATIONSAPPLICABLETOTHESEREQUIREMENTS

    NotethattheASMEcodeatonetimedistinguishedbetweenlevelindictorstypeswiththedefinitionDirectReadingforvisuallevelgagesandIndirectIndicationforallothertypesofindicators.Thatlanguagehasbeenreplacedinthecurrentcodewithsimplygageglassandremotewaterlevelindicator.

    1. I8313Allowsgaugeglasstobeisolatedwhentworemoteindicatorsused2. I8602AnewTechnologylevelindicatordoesnotreplacethevisualgage3. I8650Gageindicationfortherovingoperatorisnotequaltothecontrolroomoperator.Low

    wateralarmandtriparenotconsideredindirectindication.4. I8912Theoperatorsworkareaiswherecontrolactionsareinitiated5. I8972Anindirectleveldevicewithnopowerisnotagageglass,butcanbeconsidereda

    remotelevelindicator6. I9215Viewingagageglasswithmirrorsisconsideredadirectreading7. I9269Amagneticlevelindicatormayprovideanindirectlevelreading8. I9296Amagneticlevelindicatorisnotconsideredtobeagageglass9. I9504Apressure/temperaturecompensateddpleveltransmitterisaremotelevelindicator10. I9507ADCSCRTscreencanbearemotelevelindication.Twoareneededtoomitthegageglass,

    andtheindicationsmustbecontinuous.11. I9814Boilerswithdrumsafetyvalvessetunder400psiarenotpermittedtoshutoffthevisual

    gage,evenwithtworemoteindicatorsinoperation.

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  • FOSSILPOWERSYSTEMSINC.

    4|P a g e

    Thewaterdensityintheexternalinstrumentishigherthanthesteamdrumwaterdensity.TheexternalmeasurementinstrumentwillalwaysindicatelowerthantheTrueDrumLevel.Themagnitudeofthelevelerrordependsonoperatingpressureandheightofthewatercolumn.Thedensityofboilerwaterdecreasesasoperatingpressureincreases.Theerrorcanbesignificant,especiallyasoperatingpressuresexceed2000psi,andonlargesteamdrumswithlongvisibilitygagessuchasusedinHRSGapplications.Althoughsomeinstrumentmanufacturesmaystatethattheerrorsareinsignificantandchoosetoignorethem,theerrorsaresignificantunderconditionsofhighsteampressureandhighwaterlevels,andcannotbeignored.Thereareonlythreebasicmethodsavailabletocorrectfortheseerrors.Dependingontheleveltechnologyinuse,somemethodsaremoreorlessapplicabletovariousinstruments.Thesemethodsare:1. Heatthewaterinsidetheinstrumenttoatemperatureclosetothedrumwatertemperature.2. Physicallymovetheinstrumenttoalowerlocation.Thiswillonlyprovideacorrectionforone

    operatingpressureandforonelevelposition.Althoughformultipointlevelindicatorssuchasconductivityprobeindicators,eachprobecanbeindividuallycorrectedforagivenoperatingpressure.Correctionsarebasedonanestimateoftheinstrumentoperatingtemperature.

    3. Correcttheelectricaloutputsignal.Thisistheapproachusedforpressurecompensateddpleveltransmitters.Itcouldalsobepotentiallyusedtocorrectradarorothertypesorremoteindicatorswithanelectricaloutput.Anadditionalpressure/temperaturecorrectionsignalisusedtocorrecttheinstrumentoutputtoindicatethetruedrumlevel.

    D. LEVELINSTRUMENTSANDASSESORIES

    1. VisualLevelGages,DirectlevelMeasurementAdditionalASMERequirements:(PG60.1)Thelowestvisiblewaterlevelinagageglassshallbeatleast2abovethelowestpermissiblewaterlevel,asdeterminedbytheboilerManufacturer.(I9250)Theboilermanufacturerdeterminesthelowestpermissiblelevel(I9266)SamePG60.1definition(I8906)GageglassesarepartofBoilerExternalpiping,subjecttoPG60.WeldedgagebodiesmaybeprovidedbyamanufacturerwithoutaSection1certificate.(PG5.5)Theuseofaustenitic(series300SS)alloysteelispermittedforboilerpressurepartsthataresteamtouchedinnormaloperation.ExceptasspecificallyprovidedinPG9.1.1,PG12,andPEB5.3,theuseofsuchausteniticalloysforboilerpressurepartsthatarewaterwettedinnormalserviceisprohibited.(PG5.5note1).Austeniticalloysaresusceptibletointergranularcorrosionandstresscorrosioncrackingwhenusedinboilerapplicationsinwaterwettedservice.Factorsthataffectthesensitivitytothesemetallurgicalphenomenaareappliedorresidualstressandwaterchemistry.Susceptibilitytoattackisusuallyenhancedbyusingthematerialinastressedconditionwithaconcentrationofcorrosiveagents(e.g.chlorides,causticorreducedsulfurspecies).Forsuccessfuloperationinwaterenvironments,residualandappliedstresses

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  • FOSSILPOWERSYSTEMSINC.

    11|P a g e

    AdditionalASMERequirements(I9263)Acomputerterminalleveldisplaycanbeselectedondemand,providedthesecondremotelevelindicatoriscontinuous,withonevisualgaugeinserviceandvisibletotheoperator.(I0119)ThesamesignalalgorithmcanbeusedfortworemoteindicatorsDensityErrorConsiderations:FIGURE12Thedrumlevelindicatedtotheoperatorisacalculatedvaluebasedonthefollowingmeasurementsandassumptions:

    a. dptransmittermeasurementb. Pressuretransmittermeasurement(requiredforpressurecorrection)c. Referencelegheightd. Referencelegtemperaturee. Variablelegtemperaturef. Steamandwaterdensitycalculationattheoperatingpressure

    FIGURE12

    Significantlevelindicationerrorsareintroducedwhentheassumptionsusedinthelevelcalculationformulasdonotagreewiththeactualparameters.Errorsarealsointroducedduetoinstallationmistakes.Thesensinglinesfromtheboilertothedpinstrumentshouldbeslopedtopreventformationofgaspocketsanderroneouslevelreadings.Toobtainthebestaccuracy,temperaturesinthereferenceandvariablelegsmustaccuratelyestimated.FIGURE12showstheidealdptransmitterinstallationthatintroducestheminimumnumberofvariablesintotherequiredequations.

    LP= H1D1 + H2D2 + H4D4HP= H3D3 + H4D4DP= HP - LPDP= (H3D3 + H4D4) - (H1D1 + H2D2 + H4D4)DP= H3D3 - H1D1 - H2D2

    D1= STEAM DENSITYD2= DRUM WATER DENSITYD3= REFERENCE LEG DENSITY NOTE: DISTANCE X MUST BE SUFFICIENT SO

    THAT T IS AT AMBIENT TEMPRATURE

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  • FOSSILPOWERSYSTEMSINC.

    13|P a g e

    FromFIGURE12,Theformulaforthetransmitterdpis:1) Dp=H3D3H1D1H2D1Notethat:H1=H3H2ReplacingH1intheDpformula,theformulacanbesimplifiedas:2) Dp=[H3(D3D1)+H2(D1D2)]/62.3IftheDpisknown,theheightofwaterinthedrumcanbecalculatedfrom:3) H2=[62.3(DP)H3(D3D1)]/D1D2

    Theunitsintheseformulasare:DpinchesofwaterpressureHeight(H):InchesDensity(D):lb/ft3Conversionfactor:62.3

    EXAMPLE1:Referencelegtemperaturelowerthanestimated.Comparelines1,4,andline5intheTABLE1.Theassumptionsare:Steamdrumpressure:2500psiaReflegheight,H3,48inchesReferencelegtemperature:120FDrumwaterlevel,H2,36inchesThecalculateddpmeasurementis25.86inchesofwater(TABLEline1).Thisisconfirmedinline4.Ifthemeasureddpis25.86,thecalculateddrumlevel(H2)is36.01But,iftheactualreferencelegtemperatureis50Finsteadoftheassumed120F,theeffectofthiserrorisshowninline5ofthetable.Withthedptransmittermaintainingdrumlevelcontrolat25.86,theactualdrumlevelwillbeat37.24.Anerrorof1.23.EXAMPLE2:Nopressurecompensationofthedptransmitter.Assumethesameconditionsasabove,withthedptransmittersettomaintainadrumlevelof36whentheboilerisat2500psi.(Line1andline4).Ifnopressurecompensationwasavailableduringboilerstartup(Tableline6),atadrumpressureof20psithedrumwaterlevelwouldbeat22.72,anerrorof13.3.

  • FOSSILPOWERSYSTEMSINC.

    14|P a g e

    EXAMPLE3:DPtransmittervariablelegconnectedtothebottomofthedrum.TheFIGURE14belowshowsthisinstallationmethod.

    FIGURE14.Variablelegoffbottomofdrum

    Assumingthesameboilerconditionsasthefirsttwoexamples,butH2drumlevelnowincludestheYcomponentthatwillbeatalowertemperaturethanthesteamdrumwatersaturationtemperature.AssumeforthisinstallationthatYis12inches,andthiswaterinthislineissubcooled100Fbelowthesaturateddrumwatertemperature(waterat565F).TheeffectofthischangeisshowninLines#3and#7.ThedrumlevelfromLine#7willbethetotalofYandthecalculatedH2,or28.25.Thisisanerrorof7.75fromthesetpoint(36).

    5. MagneticFloatIndicators.FIGURE15.Thesedevicesconsistofastainlesssteel(orothernon

    magneticmaterial)pipechamberandaninternalfloat.Thefloatisalsononmagnetic,butcontainsaringofmagnets.Themagnetswithinthefloatoperateamagneticindicatorlocatedontheoutsideofthepressurechamber.Theindicatoriseitherasinglefollower,oraseriesofflagsthatrotateandchangecolourasthefloatmagnetspassby.Thefloatmagneticringwillcollectcorrosionparticles(iron/steel)fromthewaterandthefloatmustberemovedandcleanedperiodically,dependingonwaterquality.Floatsmustbecomelargeraspressureincreasesduetothereductioninwaterdensity.

    LP= H1D1 + H2D2 + H4D4HP= H3D3 + H4D4DP= HP - LPDP= (H3D3 + H4D4) - (H1D1 + H2D2 + H4D4)DP= H3D3 - H1D1 - H2D2

    D1= STEAM DENSITYD2= DRUM WATER DENSITYD3= REFERENCE LEG DENSITY

  • FOSSILPOWERSYSTEMSINC.

    15|P a g e

    FIGURE15

    AdditionalASMERequirements:(PG60.1.1.4)IndependentremotelevelindicatorsthatcontainsensingdevicesthatincludeamagneticallycoupledfloatinsideanonmagneticcylindricalpressurechambertoutilizethroughthewallsensingoffloatpositionshallberestrictedtotherequirementsofPG12.2.Thedesignandconstructionofsuchdevicesshallincludeprovisionsforeaseofcleaningandmaintenance.Attachmentofanycontroldevicesforuseotherthanindicatingwaterlevelisprohibited.(PG12.2)Boilershavingamaximumallowableworkingpressurenotexceeding900psi(6MPa)mayusealternativemethodsforindependentremotewaterlevelindicatorsorwaterlevelsensingdevices(seePG60).Thesensingdevicesmayincludeamagneticallycoupledfloatinsideanonmagneticcylindricalpressurechambertoutilizethroughthewallsensingoffloatposition.ThepressurechamberstressesshallmeettheappropriaterequirementsofPG27andPartPW,andshallberestrictedtothematerialgradeslistedinPG12.3DensityErrorConsiderations:Aswithothermanometertypeindicators,thedifferenceindensitybetweenthewaterinthedrumandthewaterinthemagneticfloatcolumnwillcausealevelindicationerror.Theerrorincreasesasthemeasuredlevelincreases.Higherpressuresandlongervisibilitieswillcreatelargererrors.Itispossibletocorrectforthiserroratoneoperatingpressureandoneindicatedlevel(typicallythezeroposition)by

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    17|P a g e

    6. GuidedWaveRadarLevelIndicators.FIGURE17Comparedwiththeothertechnologiesinuse,thisoneisrelativelynew.Guidedwavetechnologysendsaradarpulsedownaprobeinstalledinanexternalcolumn.Thepulsereflectsoffthesurfaceofthewaterbackuptheprobeandtothesensor.Thetransittimeistranslatedintoadistance,andbasedondimensionsoftheinstallation,thewaterleveliscalculated.Thisdeviceproducesacontinuousreading(420mAsignal)ofthewaterlevel.Theadvantageofthismethodoverothertypesofradarsensorsisthattheprobeguidestheradarpulseandconcentratesboththepulseandthereturnsignalenergy.Effectivelytransmittingtheradarpulsethroughthelongguideandthroughthepressurecontainmentboundarytotheelectronicsrequiresspecializedsealsandconstruction.

    FIGURE17

    DensityErrorConsiderations.Aswithotherdevicesusingawatercolumnconnectedtothesteamdrum,thewaterinthecolumnwillbecolderandconsequentlyatalowerlevelthanthesteamdrumtemperature.Iftheactualwatertemperatureinthecolumnismeasured,itwouldbepossiblefortheelectronicstocalculateandapplyacorrectionfactortotheindicatedlevel.Anadditionalconsiderationaffectingindicationaccuracyisthesignificantchangethatoccursindielectricconstantsofwaterandsteamaspressureandtemperaturechanges.Theradarpulsereflectionisactuallycausedbydetectingtheimpedancechangebetweenthewaterandsteam.Anychangeinthesevalueswillaffectthepulsetransittime,andtheindicatedlevel.Thetablebelowshowsthisaffect.

  • FOSSILPOWERSYSTEMSINC.

    18|P a g e

    TEMP(F) PRESSURE

    (PSIA)LIQDENS.(LB/FT3)

    VAPORDENSITY(LB/FT3)

    DIELECTRICCONS,LIQ

    DIELECTRICCONS,VAP

    ERROR %

    100 0 61.99 0.0029 73.95 1.001 0.0400 247 53.65 0.537 34 1.069 3.4600 1543 42.32 3.74 18.04 1.461 21

    ThedielectricconstantsofWaterandSteamapproacheachotheraspressureincreases.Programswithintheelectronicscancompensateforthischangeandmaintainthelevelindicationaccuracy.

    E. CONCLUSION

    TheASMEBoilerandPressureVesselCodeliststherequirementsforsteamdrumlevelgaugesandindicatorstoensuresafeoperationoftheboiler.Directreadingvisuallevelgaugesarerequiredoneveryboiler.Thesecanbecomplimentedwithotherindirectinstrumentstoattainthegoalofsafeandefficientboileroperation.Buttoattainthisgoal,instrumentsmustbeproperlyselectedforthedesignconditions,installedproperly,calibratedproperly,andmaintained.Ifanyoneoftheserequirementsisignored,performancewillbedegraded.Allinstrumentshaveinherentstrengthsandweaknessesbasedonthetechnologyemployedtomeasurelevel.Theseinstrumentcharacteristicsshouldbethoroughlyunderstoodbytheuser,orindicationswillbemisleading.Aprudentandconservativeapproachistousesomecombinationofthedifferentproventechnologies.Theindependentindicationstheseinstrumentsgivewillthenprovideconfidencethattheboilerisalwaysoperatedinasafecondition.

    F. REFERENCES1. Liptak,BelaG.,InstrumentEngineersHandbook,ThirdEdition19692. Kalix,D.A,DensityLevelErrorandItsCorrectioninBoilerDrumLevelIndication,ISA

    ConferenceOctober19953. Boyes,W.SomeThingsdoexactlywhattheyaresupposedto,ControlMagazineFeb20044. Evely,D.P.,HeatRecoverySteamGeneratorDrumLevelMeasurementSourcesofError,ISA

    jointPOWID/EPRIconference,20045. Gilman,J.BoilerDrumLevelControl,ISAJuly/August2010

    DavidKalix,P.E.CopyrightC2011FossilPowerSystems,Inc.FossilPowerSystemsInc.AllRightsReserved10MosherDrive,Dartmouth,27July2011NovaScotia,CanadaB3B1N5(902)4682743