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A Real-Time Approach to Process Control PDF

362 Pages·2014·4.848 MB·English
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A Real-Time Approach to Process Control Third Edition William Y. Svrcek Donald P. Mahoney Brent R. Young A Real-Time Approach to Process Control A Real-Time Approach to Process Control Third Edition WILLIAM Y. SVRCEK Department of Chemical and Petroleum Engineering, University of Calgary, Canada DONALD P. MAHONEY Chemical Industry Business Solutions, SAP AG, USA BRENT R. YOUNG Department of Chemical and Materials Engineering, University of Auckland, New Zealand Thiseditionfirstpublished2014 (cid:2)C 2014JohnWiley&Sons,Ltd Registeredoffice JohnWiley&SonsLtd,TheAtrium,SouthernGate,Chichester,WestSussex,PO198SQ,UnitedKingdom Fordetailsofourglobaleditorialoffices,forcustomerservicesandforinformationabouthowtoapplyforpermissiontoreuse thecopyrightmaterialinthisbookpleaseseeourwebsiteatwww.wiley.com. TherightoftheauthortobeidentifiedastheauthorofthisworkhasbeenassertedinaccordancewiththeCopyright,Designs andPatentsAct1988. Allrightsreserved.Nopartofthispublicationmaybereproduced,storedinaretrievalsystem,ortransmitted,inanyformorby anymeans,electronic,mechanical,photocopying,recordingorotherwise,exceptaspermittedbytheUKCopyright,Designsand PatentsAct1988,withoutthepriorpermissionofthepublisher. Wileyalsopublishesitsbooksinavarietyofelectronicformats.Somecontentthatappearsinprintmaynotbeavailablein electronicbooks. Designationsusedbycompaniestodistinguishtheirproductsareoftenclaimedastrademarks.Allbrandnamesandproduct namesusedinthisbookaretradenames,servicemarks,trademarksorregisteredtrademarksoftheirrespectiveowners.The publisherisnotassociatedwithanyproductorvendormentionedinthisbook. LimitofLiability/DisclaimerofWarranty:Whilethepublisherandauthorhaveusedtheirbesteffortsinpreparingthisbook, theymakenorepresentationsorwarrantieswithrespecttotheaccuracyorcompletenessofthecontentsofthisbookand specificallydisclaimanyimpliedwarrantiesofmerchantabilityorfitnessforaparticularpurpose.Itissoldontheunderstanding thatthepublisherisnotengagedinrenderingprofessionalservicesandneitherthepublishernortheauthorshallbeliablefor damagesarisingherefrom.Ifprofessionaladviceorotherexpertassistanceisrequired,theservicesofacompetentprofessional shouldbesought. Theadviceandstrategiescontainedhereinmaynotbesuitableforeverysituation.Inviewofongoingresearch,equipment modifications,changesingovernmentalregulations,andtheconstantflowofinformationrelatingtotheuseofexperimental reagents,equipment,anddevices,thereaderisurgedtoreviewandevaluatetheinformationprovidedinthepackageinsertor instructionsforeachchemical,pieceofequipment,reagent,ordevicefor,amongotherthings,anychangesintheinstructionsor indicationofusageandforaddedwarningsandprecautions.ThefactthatanorganizationorWebsiteisreferredtointhisworkas acitationand/orapotentialsourceoffurtherinformationdoesnotmeanthattheauthororthepublisherendorsestheinformation theorganizationorWebsitemayprovideorrecommendationsitmaymake.Further,readersshouldbeawarethatInternet Websiteslistedinthisworkmayhavechangedordisappearedbetweenwhenthisworkwaswrittenandwhenitisread.No warrantymaybecreatedorextendedbyanypromotionalstatementsforthiswork.Neitherthepublishernortheauthorshallbe liableforanydamagesarisingherefrom. LibraryofCongressCataloging-in-PublicationData Svrcek,WilliamY. Areal-timeapproachtoprocesscontrol/WilliamY.Svrcek,DonaldP.Mahoney,BrentR.Young.–Thirdedition. pagescm Includesindex. ISBN978-1-119-99387-2(cloth)–ISBN978-1-119-99388-9(pbk.)1.Processcontrol–Dataprocessing. 2.Real-timecontrol.I.Mahoney,DonaldP.II.Young,BrentR.III.Title. TS156.8.S862014 670.42(cid:3)75433–dc23 2013030739 AcataloguerecordforthisbookisavailablefromtheBritishLibrary. HBISBN:9781119993872 PBISBN:9781119993889 Setin10/12ptTimesbyAptaraInc.,NewDelhi,India. 1 2014 Contents AuthorBiographies xi ForewordandEndorsements xiii Preface xv Acknowledgements xvii 1 ABriefHistoryofProcessControlandProcessSimulation 1 1.1 ProcessControl 1 1.2 ProcessSimulation 5 References 11 2 ProcessControlHardwareFundamentals 15 2.1 ControlSystemComponents 15 2.2 PrimaryElements 16 2.2.1 PressureMeasurement 17 2.2.2 LevelMeasurement 21 2.2.3 TemperatureMeasurement 23 2.2.4 FlowMeasurement 26 2.2.5 QualityMeasurementandAnalyticalInstrumentation 32 2.2.6 ApplicationRangeandAccuracyofDifferentSensors 33 2.3 FinalControlElements 33 2.3.1 ControlValves 33 References 53 3 FundamentalsofSingle-Input/Single-OutputSystems 55 3.1 OpenLoopControl 55 3.2 Disturbances 56 3.3 FeedbackControl–Overview 57 3.4 FeedbackControl–ACloserLook 60 3.4.1 PositiveandNegativeFeedbacks 60 3.4.2 ControlElements 60 3.4.3 Sensor/Transmitter 63 3.4.4 Processes 63 3.4.5 FinalControlElement 65 3.4.6 Controller 65 vi Contents 3.5 ProcessAttributes–CapacitanceandDeadTime 66 3.5.1 Capacitance 67 3.5.2 DeadTime 71 3.6 ProcessDynamicResponse 74 3.7 ProcessModellingandSimulation 76 3.7.1 First-OrderSystems 76 3.7.2 Second-OrderandHigherOrderSystems 76 3.7.3 SimpleSystemAnalysis 83 3.7.4 ClassicalModellingforControlApproaches 89 3.7.5 TheModernModellingforControlApproach 92 References 93 4 BasicControlModes 95 4.1 On–OffControl 95 4.2 Proportional(P-Only)Control 97 4.3 Integral(I-Only)Control 102 4.4 ProportionalPlusIntegral(PI)Control 105 4.5 DerivativeAction 107 4.6 ProportionalPlusDerivative(PD)Controller 108 4.7 ProportionalIntegralDerivative(PID)Control 111 4.8 DigitalElectronicControllerForms 112 4.9 ChoosingtheCorrectController 112 4.10 ControllerHardware 114 References 117 5 TuningFeedbackControllers 119 5.1 QualityofControlandOptimization 119 5.1.1 ControllerResponse 120 5.1.2 ErrorPerformanceCriteria 122 5.2 TuningMethods 123 5.2.1 ‘TrialandError’Method 124 5.2.2 ProcessReactionCurveMethods 125 5.2.3 ConstantCyclingMethods 127 References 132 6 AdvancedTopicsinClassicalAutomaticControl 133 6.1 CascadeControl 133 6.1.1 StartingupaCascadeSystem 136 6.2 FeedforwardControl 137 6.3 RatioControl 140 6.4 OverrideControl(AutoSelectors) 142 6.4.1 ProtectionofEquipment 143 6.4.2 Auctioneering 145 6.4.3 RedundantInstrumentation 145 6.4.4 ArtificialMeasurements 147 6.5 SplitRangeControl 147 References 149 Contents vii 7 CommonControlLoops 151 7.1 FlowLoops 151 7.2 LiquidPressureLoops 153 7.3 LiquidLevelControl 155 7.3.1 Proportional-OnlyControlforIntegratingProcesses 163 7.3.2 PIControllerTuningforIntegratingProcess 164 7.4 GasPressureLoops 165 7.5 TemperatureControlLoops 166 7.5.1 TheEndothermicReactorTemperatureControlLoop 168 7.5.2 TheExothermicReactorTemperatureControlLoop 170 7.6 PumpControl 172 7.7 CompressorControl 172 7.7.1 ReciprocatingCompressorControl 173 7.7.2 CentrifugalCompressorControl 173 7.8 BoilerControl 179 7.8.1 CombustionControl 180 7.8.2 WaterDrumLevelControl 181 7.8.3 WaterDrumPressureControl 181 7.8.4 SteamTemperatureControl 181 References 182 8 DistillationColumnControl 185 8.1 BasicTerms 185 8.2 Steady-StateandDynamicDegreesofFreedom 186 8.3 ControlSystemObjectivesandDesignConsiderations 188 8.4 MethodologyforSelectionofaControllerStructure 190 8.5 Level,Pressure,TemperatureandCompositionControl 192 8.5.1 LevelControl 192 8.5.2 PressureControl 193 8.5.3 TemperatureControl 198 8.5.4 CompositionControl 198 8.6 OptimizingControl 199 8.6.1 Example:BenzeneColumnwithaRectifying SectionSidestream 199 8.7 DistillationControlSchemeDesignUsingSteady-StateModels 204 8.7.1 ScreeningControlStrategiesviaSteady-StateSimulation 206 8.7.2 ACaseStudy–TheWorkshopStabilizer 207 8.7.3 RespecifyingSimulationSpecifications 207 8.7.4 MimickingtheBehaviourofAnalysersorLabAnalyses 209 8.7.5 DevelopinganEconomicProfitabilityFunction 209 8.7.6 EvaluatingtheCandidateStrategies 210 8.7.7 EvaluatingtheCandidateStrategiesunderDisturbances 211 8.7.8 EvaluatingSensorStrategies 211 8.7.9 ExampleSummary 212 8.8 DistillationControlSchemeDesignUsingDynamicModels 212 References 213 viii Contents 9 UsingSteady-StateMethodsinaMulti-loopControlScheme 215 9.1 VariablePairing 215 9.2 TheRelativeGainArray 216 9.2.1 CalculatingtheRGAwithExperiments 216 9.2.2 CalculatingtheRGAUsingtheSteady-StateGainMatrix 218 9.2.3 InterpretingtheRGA 219 9.3 NiederlinskiIndex 220 9.4 DecouplingControlLoops 220 9.4.1 SingularValueDecomposition 221 9.5 TuningtheControllersforMulti-loopSystems 222 9.6 PracticalExamples 222 9.6.1 Example1:ATwo-StreamMixer 222 9.6.2 Example2:AConventionalDistillationColumn 226 9.7 Summary 232 References 232 10 Plant-WideControl 233 10.1 Short-TermversusLong-TermControlFocus 233 10.2 CascadedUnits 235 10.3 RecycleStreams 236 10.4 GeneralConsiderationsforPlant-WideControl 241 References 242 11 AdvancedProcessControl 245 11.1 AdvancedProcessControl 245 11.2 ModelPredictiveControl 246 11.3 DynamicMatrixControl 249 11.4 GeneralConsiderationsforModelPredictiveControlImplementation 253 References 254 AppendixA P&IDSymbols 257 AppendixB GlossaryofTerms 261 AppendixC NewCapabilitieswithControlTechnologyHardware andSoftware 267 Workshop1 LearningthroughDoing 279 Workshop2 FeedbackControlLoopConcepts 283 Workshop3 ProcessCapacityandDeadTime 289 Workshop4 FeedbackControl 295 Workshop5 ControllerTuningforCapacityandDeadTimeProcesses 303

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