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Offshore Oil and Gas Production Systems

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Offshore Oil and Gas Production

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  • OffshoreOilandGasProductionSystems

  • SBM

    UMBILICAL(DATA/WELLCONTROL) OILTOREFINERY

    WELLFLUID OIL

    INJ.WATER GAS GASTOCONSUMERS

    LIFTGAS

    WELLS WELLS WELLS/CONNECTEDWELLP/FOILPRODUCERS WELLTESTING SEPARATIONMODULEOIL/GAS/WATER

    GASPRODUCERS PRODNOPTIMIZATION GASCOMPRESSIONANDDEHYDRATIONMODULE

    INJECTIONWELLS WELLCONTROL SEAWATERTREATMENTFORWATERINJECTION

    WELLSERVICING PRODUCEDWATERTREATEMENTMODULE

    TELEMETRY/SCADA POWERGENERATION

    UTILITIESWATER/SUPPLIES

    LIVINGQUARTERS

    DRILLING/WELLSERVICINGRIGMODULE

    WELLFLUID(OIL/GAS/WATER)

    INJETCTIONWATER

    LIFTGAS

    DATA/SCADA

    POWER

    OFFSHOREPRODUCTIONSYSTEMASCHEMATIC

    W

    WELLP/F'SPROCESS

    PLATFORMSONSHORETERMINALS

    TANKER

  • THEMAJORELEMENTSOFOFFSHOREPRODUCTIONSYSTEM

    WELLS(SUBSEA/PLATFORMWELLS)

    WELLPLATFORMS/WELLSERVICINGRIGS

    FEEDERSUBSEAPIPELINES

    PROCESSINGPLATFORMS

    EXPORTPIPELINESFOROIL/GAS

    TANKERSFOREVACUATIONOFOIL.

  • Weshalldiscussabout

    PLATFORMS WELLHEADPLATFORMS WELLS PROCESSINGSYSTEM NEWTECHNOLOGIES

  • TYPESOFOFFSHOREPLATFORMS

  • WATERDEPTHANDTYPEOFPLATFORM

  • Oilplatforms Anoilplatformoroilrigisalargestructureusedtohouse

    workersandmachineryneededtodrilland/orextractoilandnaturalgasthroughwellsintheoceanbed.

    Dependingonthecircumstances,theplatformmaybeattachedtotheoceanfloor,consistofanartificialisland,orbefloating.

    Generally,oilplatformsarelocatedonthecontinentalshelf,thoughastechnologyimproves,drillingandproductionindeeperwatersbecomesbothfeasibleandprofitable.

    Atypicalplatformmayhavearoundthirtywellheadslocatedontheplatformanddirectionaldrillingallowsreservoirstobeaccessedatbothdifferentdepthsandatremotepositionsupto5miles(8kilometres)fromtheplatform.

    Manyplatformsalsohaveremotewellheadsattachedbyumbilicalconnections,thesemaybesinglewellsoramanifoldcentreformultiplewells.

  • FIXEDPLATFORMSTheseplatformsarebuiltonconcreteand/orsteellegsanchoreddirectlyontotheseabed,supportingadeckwithspacefordrillingrigs,productionfacilitiesandcrewquarters.

    Suchplatformsare,byvirtueoftheirimmobility,designedforverylongtermuse.

    Varioustypesofstructureareused,steeljacket,concretecaisson,floatingsteelandevenfloatingconcrete.

    Steeljacketsareverticalsectionsmadeoftubularsteelmembers,andareusuallypiledintotheseabed.Concretecaissonstructures,oftenhaveinbuiltoilstorageintanksbelowtheseasurfaceandthesetankswereoftenusedasaflotationcapability,allowingthemtobebuiltclosetoshoreandthenfloatedtotheirfinalpositionwheretheyaresunktotheseabed.

    Fixedplatformsareeconomicallyfeasibleforinstallationinwaterdepthsuptoabout1,700feet(520m).

  • FixedPlatform

  • SemisubmersiblePlatformTheseplatformshavelegsofsufficientbuoyancytocausethestructuretofloat,butofweightsufficienttokeepthestructureupright.

    Semisubmersiblerigscanbemovedfromplacetoplace;canbeballastedupordownbyalteringtheamountoffloodinginbuoyancytanks;

    Theyaregenerallyanchoredbywithchain,wireropeand/orpolyesterropeduringdrillingoperations,thoughtheycanalsobekeptinplacebytheuseofdynamicpositioning.

    Semisubmersiblescanbeusedinwaterdepthsfrom200to10,000feet(60to3,050m).

  • JackupPlatformsJackups,asthenamesuggests,areplatformsthatcanbejackedupabovetheseausinglegswhichcanbeloweredlikejacks.

    Theseplatformsaretypicallyusedinwaterdepthsupto400feet,althoughsomedesignscangoto550feetdepth.

    Theyaredesignedtomovefromplacetoplace,andthenanchorthemselvesbydeployingthelegstotheoceanbottomusingarackandpiniongearsystemoneachleg.

  • CompliantTowers

    Theseplatformsconsistofnarrow,flexibletowersandapiledfoundationsupportingaconventionaldeckfordrillingandproductionoperations.Complianttowersaredesignedtosustainsignificantlateraldeflectionsandforces,andaretypicallyusedinwaterdepthsrangingfrom1,500and3,000feet(450and900m).

  • Drillships

    Adrillshipisamaritimevesselthathasbeenfittedwithdrillingapparatus.Itismostoftenusedforexploratorydrillingofnewoilorgaswellsindeepwaterbutcanalsobeusedforscientificdrilling.Earlyversionswerebuiltonamodifiedtankerhull,butpurposebuiltdesignsareusedtoday.Mostdrillshipsareoutfittedwithadynamicpositioningsystemtomaintainpositionoverthewell.Theycandrillinwaterdepthsupto12,000feet(3,660m).

  • FloatingproductionsystemsFPSOsarelargeshipsequippedwithprocessingfacilitiesandmooredtoalocationforalongperiod.

    Themaintypesoffloatingproductionsystemsare:

    FPSO (floatingproduction,storage,andoffloadingsystem),

    FSO (floatingstorageandoffloadingsystem),and

    FSU (floatingstorageunit).

    Theseshipsdonotactuallydrillforoilorgas.

  • FPSOANDSUBSEAWELLS

  • TensionlegplatformTLPsconsistoffloatingrigstetheredtotheseabedinamannerthateliminatesmostoftheverticalmovementofthestructure.

    TLPSareusedinwaterdepthsuptoabout6,000feet(2,000m).The"conventional"TLPisa4columndesignwhichlookssimilartoasemisubmersible.

    ProprietaryversionsincludetheSeastarandMOSESminiTLPs;theyarerelativelylowcost,usedinwaterdepthsbetween600and4,300feet(200and1,300m).

    MiniTLPscanalsobeusedasutility,satelliteorearlyproductionplatformsforlargerdeepwaterdiscoveries.

  • SPARPlatformsSparsaremooredtotheseabedliketheTLP,butwhereastheTLPhasverticaltensiontetherstheSparhasmoreconventionalmooringlines.

    Sparshavebeendesignedinthreeconfigurations:the"conventional"onepiececylindricalhull,the"trussspar"wherethemidsectioniscomposedoftrusselementsconnectingtheupperbuoyanthull(calledahardtank)withthebottomsofttankcontainingpermanentballast,andthe"cellspar"whichisbuiltfrommultipleverticalcylinders.

    TheSparmaybemoreeconomicaltobuildforsmallandmediumsizedrigsthantheTLP,andhasmoreinherentstabilitythanaTLPsinceithasalargecounterweightatthebottomanddoesnotdependonthemooringtoholditupright.

    Italsohastheability,byuseofchainjacksattachedtothemooringlines,tomovehorizontallyovertheoilfield.

    Worldsdeepestspar:Eni'sDevil'sTowerislocatedin5,610feet(1,710m)ofwater,intheGulfofMexico;however,whenShell'sPerdidoSparisinstalled,itwillbethedeepestat8,000feet(2,438m

  • Maintenanceandsupply Atypicaloilproductionplatformisselfsufficientinenergyandwaterneeds,

    housingelectricalgeneration,waterdesalinatorsandallofthe equipmentnecessarytoprocessoilandgassuchthatitcanbeeitherdelivereddirectlyonshorebypipelineortoaFloatingStorageUnitand/ortankerloadingfacility.

    Elementsintheoil/gasproductionprocessincludewellhead,productionmanifold,Productionseparator,glycolprocesstodrygas,gascompressors,waterinjectionpumps,oil/gasexportmeteringandmainoilline pumps.

    Allproductionfacilitiesaredesignedtohaveminimalenvironmentalimpact.

    LargerplatformsareassistedbysmallerESVs(emergencysupport vessels)thataresummonedwhensomethinghasgonewrong,e.g.whenasearchandrescueoperationisrequired.

    Duringnormaloperations,PSVs(platformsupplyvessels)keeptheplatformsprovisionedandsupplied,andAHTSvesselscanalsosupplythem, aswellastowthemtolocationandserveasstandbyrescueandfirefightingvessels.

  • Crew Thesizeandcompositionofthecrewofanoffshore

    installationwillvarygreatlyfromplatformtoplatform.

    Becauseofthecostintensivenatureofoperatinganoffshoreplatform,itisimportanttomaximiseproductivitybyensuringworkcontinues24hoursaday.

    Thismeansthatthereareessentiallytwocompletecrewsonboardatatime,onefordayshiftandtheotherfornightshift.Crewswillalsochangeoutatregularintervals,nominallytwoweeks.

  • Essentialpersonnel Notallofthesepersonnelarepresentoneveryplatform,onsmallerplatformsworkerswillberesponsible

    forseveralareas.Thenamesshownarenotindustrywide.

    * OIM(offshoreinstallationmanager)istheultimateauthorityduringhis/hershiftandmakestheessentialdecisionsregardingtheoperationoftheplatform.

    * OperationsTeamLeader(OTL)* OffshoreOperationsEngineer(OOE)istheseniortechnicalauthorityontheplatform* PSTLorOperationscoordinatorformanagingcrewchanges* DynamicPositioningOperator,navigation,shiporvesselmaneuvering(MODU),stationkeeping,

    fireandgassystemsoperationsintheeventofincident* 2ndMate Meetsmanningrequirementsofflagstate,operatesFastRescuecraft,cargoops,fire

    teamleader.* 3rdMate Meetsmanningrequirementsofflagstate,operatesFastRescuecraft,cargoops,fire

    teamleader* BallastControlOperator_alsofireandgassystemsoperator* Craneoperatorstooperatethecranesforliftingcargoaroundtheplatformandbetweenboats.* Scaffolderstorigupscaffoldingforwhenitisrequiredforworkerstoworkatheight.* Coxwainsformaintainingthelifeboatsandmanningthemifnecessary.* Controlroomoperators EspeciallyFPSOorProductionplatforms.* Cateringcrewwillincludepeopletaskedwithperformingessentialfunctionssuchascooking,

    laundryandcleaningtheaccommodation.* Productiontechsforrunningtheproductionplant* HelicopterPilot(s)liveonsomeplatformsthathaveahelicopterbasedoffshore.Thehelicopter

    flightcrewtransportsworkerstootherplatformsortoshoreon crewchanges.* maintenancetechnicians(instrument,electrical,mechanical)

  • MANAGERS: OFFSHOREINATALLATIONMANAGER PROCESSMANAGER MAINTENANCEMANAGER WELLPLATFORMMANAGER HSEMANAGER

    TEAMS Processcontrolroomoperators Mechanical/Electrical/Instrumentationteam StaticEquipmentmaintenanceteam Wellheadteams Pipelinemaintenanceteam SkilledandUnskilledtechnicians

    Essentialpersonnel ONGCSystem

  • Incidentalpersonnel* Drillcrewwillbeonboardiftheinstallationisperforming drillingoperations.Adrillcrewwillnormallycomprise:

    oToolpusheroRoughnecksoRoustaboutsoCompanymanoMudengineeroDerrickhandoGeologist

    * Wellservicescrewwillbeonboardforwellwork.Thecrewwillnormallycomprise:

    oWellservicessupervisoroWirelineorcoiledtubingoperatorsoPumpoperator

  • Risks Thenatureoftheiroperation extractionofvolatilesubstances

    sometimesunderextremepressureinahostileenvironment hasriskandaccidentsandtragediesoccasionallyoccur.InJuly1988,167peoplediedwhenOccidentalPetroleum'sPiperAlphaoffshoreproductionplatform,onthePiperfieldintheNorthSea,explodedafteragasleak.Theaccidentgreatlyacceleratedthepracticeofprovidinglivingaccommodationsonseparaterigs,awayfromthoseusedforextraction.

    However,thiswas,initself,ahazardousenvironment.InMarch1980,the'flotel'(floatinghotel)platformAlexanderKiellandcapsizedinastormintheNorthSeawiththelossof123lives.

    Giventhenumberofgrievancesandconspiracytheoriesthatinvolvetheoilbusiness,andtheimportanceofgas/oilplatformstotheeconomy,platformsarebelievedtobepotentialterroristtargets.AgenciesandmilitaryunitsresponsibleformaritimeSecurityoftentrainforplatformraids.

  • Ecologicaleffects InBritishwaters,thecostofremovingallplatformrigstructuresentirelywasestimatedin

    1995at$345billion,andthecostofremovingallstructuresincludingpipelines asocalled"cleansea"approach at$621billion.

    Furthereffectsaretheleachingofheavymetalsthataccumulate inbuoyancytanksintowater;andrisksassociatedwiththeirdisposal.

    Therehasbeenconcernexpressedatthepracticeofpartiallydemolishingoffshorerigstothepointthatshipscantraverseacrosstheirsite;therehavebeeninstancesoffisheryvesselssnaggingnetsontheremainingstructures.

    ProposalsforthedisposalatseaoftheBrentSpar,a449fttallstoragebuoy,wasforatimein1996anenvironmentalcauseclbreintheUKafterGreenpeaceoccupiedthefloatingstructure.Theeventledtoareconsiderationofdisposalpolicy intheUKandEurope.

    IntheUnitedStates,MarineBiologistMiltonLovehasproposedthatoilplatformsofftheCaliforniacoastberetainedasartificialreefs,insteadofbeingdismantled(atgreatcost),becausehehasfoundthemtobehavensformanyofthespeciesoffishwhichareotherwisedecliningintheregion,inthecourseof11yearsofresearch.Loveisfundedmainlybygovernmentagencies,butalsoinsmallpartbytheCaliforniaArtificialReefEnhancementProgram.

    IntheGulfofMexico,morethan200platformshavebeensimilarlyconverted.

  • UnUn--manned Platformsmanned Platforms

  • Normallyunmannedinstallations.

    Theseinstallations(calledWellheadPlatforms),aresmallplatforms,consistingoflittlemorethanawellbay,helipadandemergencyshelter.

    Theyaredesignedtooperateremotelyundernormaloperations,onlytobevisitedoccasionallyforroutinemaintenanceorwellwork.

  • WELLHEADPLATFORMS Generally4leggedunmannedplatforms Consistsof4decks,spiderdeck,cellardeck,maindeckandhelideck PersonnelvisittheplatformforWelltestingandothermaintenance

    activities. Mayhave3to32wells(ProducersandInjectors),oneverticalwelland

    othersdirectionalandreachingoutindifferentdirectionupto 6kmfromtheplatform.

    WellsaredrillednormallybyJackupRigsthatdockwiththeplatform. Wellservicing(workover)isdoneeitherbyJackuprigsorbyModular

    Rigsthatareassembledovertheplatform.

    JACKUPRIGDOCKEDONWELLPLATFORMFORDRILLING/WELLSERVICING

    SOLARPANELSPOWERTHEWELLPLATFORMS

  • FacilitiesinWellPlatforms Wells ProductionManifoldtoreceivewellfluidfromallthewells LiftgasManifoldforfeedingliftgastowellalongwithInjectiongas

    regulation/Controlandmeasurementsystem. WImanifoldforfeedinginjectionwatertoWIwellsalongwithmeteringsystem. TestmanifoldandTestseparatorandassociatedmeasurementsystemforOil,Gas

    andWater. WellcontrolPanel(SDP) Instrumentgassystem RTUandSCADA Batterypack,Solarpowerpanel. SubsealinescarrywellfluidfromtheplatformtotheProcessplatform Also,LiftgasandInjectionwaterisbroughtinbysubsealines fromProcess

    Platform. EmergencyGenset. FirewaterpumpsandFirefightingsystem. HCGasdetectors ESD/FSDsystem Crane.

  • SDP Pneumatic control panels are designed tomonitor crucialwellhead safety parameters.

    Theyprovidesequentialstartupandsafeshutdownofproduction wells.

    Inremoteunmannedwellheadplatformsproducedgasisusedasthemediuminsidethecontrolpanel.Easyavailabilityofpneumaticpower sourcemakes pneumatic controlsadesirablechoice.

    Thepneumaticshutdownpanelisdesignedasacentralprotection unitforoverallprotectionoftheinstallation.Threelevelsofprotectionforpersonnel,productionwellsandsurfacefacilitiesareenvisaged.Thusapanelconsistsof;

    a)Fireandgasleakageprotectionsystem:Anygasleakageisautomaticallydetectedandappropriate shutdown action initiated to prevent formation of combustible mixture. Allsources of ignition are also shutdown. Any eruption of fire is detected and appropriateshutdownandsuppressionactioninitiated.

    b)SurfaceFacilityProtection:Asafetyanalysisorhazardousoperability(HAZOP)analysisofsurfacefacilities includingrotaryandprocessequipments iscarriedout.Allpossiblehazards,interrelationbetweenvariousparametersare identifiedand listed.The functionalchartthusevolvedistheSAFE(SafetyAnalysisandFunctionEvaluation)chart.TheSAFEchartformsthebasisfordesignofpanelinsurfacesafetyprotection.

    c)Wellcontrol&Protection:Amajorfunctionofthewellheadshutdownpanelistocontrolthewellthroughthesurfaceandsubsurfacesafetyvalves.Theinterrelationsbetweenvariousvalvesarewelldefinedandtheirsequentialoperationestablished.

  • WELLCONTROLSCHEMATIC

    PNEUMATICPRESSURETOSSV

    PNEUMATICSUPPLY

    RADIO

    SIGNAL

    HYDRAULICPRESSURETOSSSV

    REMOTE

    CONTROL

    PNEUMATICSUPPLY

    WELL CONTROLSDP

    RTU(REMOTETELEMETRYUNIT)

    SURFACECONTROLLEDSUBSURFACESAFETYVALVE 150MFROMP/FDECK

    SSV SUFRACESAFETYVALVE

    GISHUTDOWNVALVE

    PRESSURESWITCHHIGHLOW

    FSD FIRESHUTDOWN FUSIBLEPLUGLOOP

    WELLFLOW

    LIFTGAS

    WELL XMASTREE

    ESD

    HCDETECTORS

  • WELLCONTROL WellsclosebySSV(SurfaceSafetyValve)andSSSV(SubsurfaceSafetyValve)whenabnormalconditionsexists.

    AbnormalconditionsmaybeHigherPressuresintheflowlines,Fire.

    WellscanalsobeclosedremotelyfromProcessplatforms/ShorethroughSCADAwiththehelpofRTU.

  • SMARTWELLHEADPLATFORMS ProvidesWellheadrealtimedata.

    ProvideRealtimeMonitoringandControlofUnmannedPlatformsandwells.

    ProvidesminimumHumanInterventionindaytodayoperations

    ProvideStabilisedproductionandTransportationsprocessalongwithOptimisations

    ProviderealtimedataConsolidation,Recordingandstoragefortheanalysisforfutureevaluations.

    ReducethedelayindecisionmakingviaonlinemeasurementsofcriticalparameterssuchasWatercut,GasRatesetc.

  • MajorElementsofSMARTplatform Instrumentationonwellhead.

    AutomatedWelltestingusingRemotelyOperatedMultiSelectorValveinwellplatform.

    AutomationsystemtoMonitorandOptimiseProduction.

    RemoteLiftGasoptimization.

    Integrationofdifferentautomationsystemtoensuredataconsolidationatcentralfacilities.

    WANCommunication:Radio,V satatoffshorewellheadplatform.

  • WELLS Producers

    Selfflow,GasliftedandESP.

    Injectors Subseawells:

    DryTree,WetTreewells.

    Directionalwells Horizontalwells ERDWells Multilateralwells Intelligentwells

  • GasLiftedwells

  • SELFFLOWINGANDGASLIFTEDWELLS

  • ELECTRICALSUBMERISBLEPUMPS(ESP)WELLS

  • VERTICAL WELL

    LI

    LII

    LIII

    S IGAS

    D

    E

    P

    T

    H

    PRESSUREOIL1800 psi

    OIL & GAS

    1350

    2050 PSI

    30

    20

    13 3/8

    7 LINER

    9 5/8

  • DIRECTIONALWELL

    LI

    LII

    LIII

    S I

    30/26

    20

    13 3/8

    9 5/8

    7

    `

    OIL

  • PRODUCING ZONE

    HORIZONTAL HORIZONTAL WELLSWELLS

    Drain hole

  • MULTIMULTI--LATERAL WELLLATERAL WELLMULTILATERALWELL

  • FISHBONEMULTILATERALWELL

    Manyribsbranchoffthemainwellbore.Thepathofoiltothewellisshorterthrougharibthanthroughtherock,bothinhomogeneous sandsandevenmoreinheterogeneoussandswithbarriersandbaffles.Ribscanbeadded toanylateral.

  • WELLMONITORINGANDCONTROLRTU/SCADA

  • SCADA FORWELLMONITORING,CONTROLANDPRODUCTIONOPTIMIZATION

    SUPERVISORYCONTROLANDDATAACQUISITION

    GathernecessaryDATAfromaREMOTELYLOCATEDOil/GaswellandWellPlatformwiththehelpofFieldTransmitters&RTUandsendittotheDATAGATHERING&ANALYSISpoint.

  • SCADA OVERVIEW

    WELLPLATFORM PROCESSPLATFORM

    RADIOLINK

    DATAGATHERINGAND

    INTERPRETATION

    LIFTGAS

    INJECTIONWATER

    WELLFLUID

  • RESERVOIR

    BHP

    WELLHEADPRESSURE&

    TEMP

    SSV

    LIFTGASFROMPROCESSPLATFORM

    GAS/OIL TOGROUPHEADER

    GIACV

    LIFTGASRATE

    GLV

    OIL,GASWATER

    FLOWRATES

    PRODUCTIONTUBING

    ANNULUS

    SCADAMETHODOLOGY

    PARAMETERSAVAILABLEFORMEASUREMENTINANOILWELLONGASLIFT

    SSSVOPEN/CLOSE

    STATUS

    GASINJ.PRESSURE

    SSVOPEN/CLOSE

    STATUS

  • MONITORINGPRESSURE,TEMPetcATSANDFACE,WELLHEADORELSEWHEREWITHTHEHELPOFSENSORS

    SCADA ASCHEMATIC

    RTUINSTALLEDONWELLPLATFORM

    (ANALOGTODIGITALCONVERSION)

    ANALOGSIGNALSINRANGEOF15V(420mA)

    RADIOLINK

    DATAGATHERINGSTATION(USUALLYAPROCESSPLATFORM)

    INTERFACINGSOFTWARE

    INTERPRETATIONOFSTOREDDATA

    DECISIONMAKINGPROCESS

  • MAJORBENEFITSOFSCADA 24hrsonlinemonitoringofwellstatusandflow,liftparametersfrom

    ProcessComplexaswellasfromonshorecontrolcentre.

    HistoricalDataandtrendinghelpsinTroubleshooting.

    Abilitytoclosewellsremotelyduringemergency.

    BetterProductionoptimizationofindividualwells

    InstantalertsincaseofWellclosures,ESD,FSDandcontrolpanelfailure

    OptimumutilizationofManpowerforattendingtowellproblems

    Reductioninnumberofphysicalvisitstowellplatformsresultingin

    optimizationofHelicoptersorties.

    Toobserveslugginginpipelines.

    Liftgasallocationforeachwell.

  • MONITORINGOFWELLPLATFORMUSINGSCADA THISISACCESSIBLEFROMANYDESKTOPCOMPUTERINONGCLANNETWORK.

    MIMICDISPLAY

  • STATUSDISPLAY

    MONITORINGOFWELLPLATFORMUSINGSCADA

  • MONITORINGDIFFERENTALARMSWITHTHEHELPOFSCADA

  • SCADAHELPSINLIFTGASALLOCATION/PRODUCTIONALLOCATION

  • TRENDINGOFGIPRESSURE,MLGIP,TEMPERATURE,LIFTGASRATEHELPS INKEEPINGWELLSFLOWINGATITSOPTIMUM24x7

  • WELLAUTOMATION

  • RESERVOIR

    PROD.CHOKE

    LIFTGASFROMPROCESSPLATFORM

    REMOTELYCONTROLLEDGIACV

    GAS/OIL

    GLV

    PRODUCTIONTUBING

    ANNULUS

    FLOWSENSORS

    OWGFTHP

    WHT

    GIP

    BHP

    BHT

    LIFTGASFLOW

    DESIGNFORAUTOMATEDCONTROLSYSTEMFORGLOPTIMIZATION

    ALGORITHMFORGASLIFTOPTIMIZATION(BASEDONGASINOILOUTCURVE)

    AUTOMATEDFEEDBACK

    CONTROLERTOMAINTAINTHEFIXED

    LIFTGASRATE

    CONTROLSIGNALFORACVTO

    ADJUSTTHELIFTGASFLOW

    GASFLOWREQUIREDFOROPTIMUM

    PRODUCTION

  • OnlineMonitoringandRemotecontrolofInjectionGas

    FT

    TTI/P

    PT

    G

    I

    H

    E

    A

    D

    E

    R

    VBGas injection to well

    RTU

    FLOW COMPUTERWith Flow control card

    FE

    TEFCV

    CVA

    SP

    FC is accessed via SCADA from the process complex and Injection gas Rate is monitored and adjusted, if required, remotely.

    RTU

  • REMOTEOPTIMIZATIONOFWELLUSINGFCMPFMSET

    FT

    TTI/P

    PT

    Gas injection to wellG

    I

    H

    E

    A

    D

    E

    R

    VB

    FLOW COMPUTERWith Flow control card

    FE

    TEFCV

    CVA

    SP

    Injection gas is remotely monitored, controlled via RTU-FC-FCV through SCADA

    One well is diverted via MPFM and Production rates available through SCADA at Process PF.

    Well can be tested and Optimized REMOTELY for different Injection gas rates by changing the set point in FC-I/P-FCV Loops via SCADA.

    WELL

    MPFM

    To header

    RTU

    RTU

  • SMARTonline24x7monitoringandOptimizationofeachwellUsingGasFlowComputer CompactGLCCSeparator CoriolisMassflowMeter Set.

    (Flowcomputer)

    ToHeader(

    RTU

    CoriolisMassFlowMeter

    GLCC(GasLiquidCylindricalCyclonic)Separator

    InjectionGascontrolledRemotelythroughSCADAbyFCFCV

    WELL

    RTU

  • JackupRigdockedinaWellheadplatform

  • PROCESSINGINOFFSHOREPROCESSPLATFORMS

    GASCOMPRESSION&DEHYDRATION

    SEAWATERTREATMENTANDINJECTION

    SEPARATIONANDCRUDEPUMPING

    BRIDGECONNECTEDWELLPLATFORM

    LIVINGQUARTERS

  • PROCESSES

    Separation(Oil,GasandProducedwater)&Oildispatch

    GasCompression&dehydration

    ProducedWaterConditioning

    Seawaterprocessing&injectionsystem

    3PhasewellfluidisreceivedfromWells/WellPlatformsandprocessedatLargeProcessPlatformsgenerallyconsistingofthefollowingfourMajorProcessingModules

    Theseprocesscomplexeswillalsohavethefollowing: Firedetection&Suppressionsystem

    PowerGeneration

    Wellservices/drillingModules

    WaterMaker/Utilities/SewageTreatment

    LivingQuarters

  • SEPARATION

  • Oil,GasandWaterisseparatedfromtheWellfluid. WellFluidfromvariousWells/WellPlatforms/SubseaManifoldreachestheprocess

    complexviasubseapipelinesandrisersandisfurtherprocessed inmorethanone

    train.

    EachTrainwillnormallyconsistofaProductionManifold,Well fluidheater,InletSeparator,CrudeoilManifold,Crudeoilheater,SurgeTanksand MOLPumps.

    WellFluidisreceivedintheProductionManifold.DemulsifierChemicalisdozedinProductionmanifoldtopromotebreakingupofWaterOilemulsion

    ThenitisheatedinwellfluidheaterwithHotoilFlowinginShellSideandwellfluidintubeside.ThisheatingenablesbetterseparationofoilandwaterinInlet

    Separator.

    TheWellFluidfromWellfluidheaterreachesInletSeparator.

    SEPARATION

  • InletSeparatorisavesselinwhich3phaseseparationofwellfluidintoOil,GasandWateroccurs.

    Separationisbygravitymainlyassistedbychemicalandheat.Residencetimeinthevesselisanimportantcriteriaforbetterseparation.

    SeparatedGasisroutedtoGascompressionanddehydrationModule. CompressedgasissenttotheLiftgasnetworkforliftingtheproducersandexcess

    gasisexportedviapipelinestoshore. Separatedoilflowstotheoilmanifold. SeparatedwaterflowstoProducedwaterconditioningunit. Fromoilmanifoldcrudeoilflowstocrudeoilheaterinwhichcrudeoilisheatedwith

    hotoil.Thisenhancestheseparationofoil&waterinSurgeTanks(secondstageseparation).

    DemulsifierchemicaldozedinoilmanifoldfurtherpromotesthebreakingofwaterOilemulsion.

    InletSeparator FirstStageSeparation

  • PFD OIL,GAS,WATERSEPARATION

  • SurgeTank SecondStageSeparation

    Surge tank ismaintainedat a lowerpressure to stabilize crude i.e. toremovemaximumofassociatedgasfromthecrudeoil.

    OilfromsurgetankscanbeeitherpumpeddirectlywithMOLpumpsorcanbedivertedtothirdstageseparators(Surgetank3).

    Separated crudeoil ispumpedwithCTP /MOLpumps toexport trunklines.

    SeparatedGasisdivertedtoGascompressionmoduleafterboostingthepressureLPboostercompressor.

    SeparatedWaterisdivertedtoProducedwaterconditioningUnit.

  • A B

    V-1210

    Separator TR A

    To Produced Water Flesh Vessel

    Gas For SalesHP FlareLP Flare

    Skimmer Oil

    HP Condensate

    WF Heater

    WF Heater

    Oil Processing

    Hot oil supply

    Hot oil supply

    E-1150

    E-1160 V-1220Separator TR B

    V-1300

    Surge tank TR A

    V-1310

    Surge tank TR B

    V-1380

    Stabilization tank

    LCV-1314B

    LCV-1304B

    E-1280

    E-1290

    Hot oil supply

    Hot oil supply

    Crude oilHeater

    Crude oilHeater

    HP Booster Compressors

    C-1470A C-1470BLP Booster Compressors

    C-1500A C-1500BI stage I stage

    II stage II stage

    LP Flare

    HP Flare

    HP Flare

    LP Flare

    LP Flare

    HP Flare

    P

    U

    M

    P

    S

    U

    C

    T

    I

    O

    N

    M

    A

    N

    I

    F

    O

    L

    D

    P=8 KSC

    P=8 KSCP=4 KSC

    P=4 KSC

    P=2.25 KSC

    TO SUMP

    A B

    P

    R

    O

    D

    U

    C

    T

    I

    O

    N

    M

    A

    N

    I

    F

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    D

    O

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    M

    A

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    I

    F

    O

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    D

    IA

    IB

    ID

    SG

    SM

    SR

    ST

    From ICD

    From ICG

    IC ISIQ SD

    ZA IU WB

    A B

    FROM / TO BHS

    FROM / TO BHS

    TO RESTART

    PUMP

    TO RESTART

    PUMP

    WELLPLATFORMS

    SEPARATIONOFOIL/GAS/WATER

  • ReturnHdr.

    TrimCoolerE2880

    HeatExchangerE2810

    HotoilExpansionTank

    FILTER

    FILTER

    P

    P

    FCV2850

    PCV2853

    HIC2811

    TIC2814

    SupplyHdr.

    TGExhaust

    PCV

    catchpot

    NITROGENBLANKETING

    TCV2881

    PIC

    TIC

    FIC

    BYPAS

    DUCT

    XSDVPCV

    PSV

    T=400C

    T=250C

    WASTEHEATRECOVERYHotOilSystem

  • Pump Suction Manifold

    Discharge Manifold

    Crude Oil Export

    CTP-1320 CTP-1330 CTP-1340 MOL-1350 MOL-1360 MOL-1370

    TR B RECYCLE TO SURGE TANKS

    TR A RECYCLE

    TR A

    TR B

    TR A

    TR B

    LCV-1304

    LCV-1384

    LCV-1314

    T/M-1

    T/M-2

    FROM/TO

    BHS

    TO HEERA

    A B

    TOONSHORE

  • CRUDEEVACUATIONBYSBMANDTANKER

  • GASCOMPRESSION,DEHYDRATIONANDEXPORT

  • GasCompression. GasfromSeparators,SurgeTanksandexportgasesifanyfromotherprocess

    platformsarecompressedtoabout90100kg/cm2pressureasperthefieldgasliftrequirement.

    NormallyGas turbinedrivenCentrifugal compressors (PGCs ProcessGasCompressors)areused.

    Gases compressed in PGCs is dehydrated to prevent formation of GASHYDRATES.Gashydratesareformedatlowtemperatureswhenmoistureispresent in Hydrocarbon gases. These gas hydrates are ice like substancewhichpreventthesmoothfloworblocktheflowofgasesingas flowlines.

    GasHydratescanbeformedinAdjustableChokeValves,PCVs&GLVsinGILines where Throttling of gases give rise to low temperatures.(JouleThomsoneffect).ThiscanaffectproductionphenomenallyfromGas liftwells.

  • P/T G LP INT HPGG

    Dehydration Manifold

    Cond.Hdr

    1st StageK.O.D

    2nd StageK.O.D

    3rd StageK.O.D

    DischargeK.O.D

    InletManifold

    Cooler Cooler Cooler

    FuelGas

    F

    F

    H

    M

    GASCOLLECTIONANDCOMPRESSION

  • Compressed Gas is dehydrated in a Glycol contactor with Tri EthyleneGlycol(TEG)asanabsorbentformoisturefromcompressedgas.

    Glycolcontactorisbubblecaptraycolumnwithmanybubblecaptrays.TEGflowscountercurrentwithcompressedgasfromthetopofthecolumn.

    TEG coming in contact with compressed gas in the bubble cap traysselectivelyabsorbsthemoisturefromthegasanddehydratesit.

    The dehydrated gas is sent to feed gas lift wells in priority basis andremainingtoexportgasline.

    TheTEG rich inmoisture is sent for reconcentration ,converted toLeanglycolandrecycledbacktocontactorfordehydration.

    GasDehydration

  • Glycol

    Contactor

    CoalescerSeparator

    GlycolScrubber

    FlashDrum GlycolStill

    GlycolStorage

    F F

    F

    BoosterPumpsCirculationPumps

    Reboiler

    HotOilSupply

    Tank

    Lean/RichGlycolExchangers

    LeanGlycol/GasExchanger

    LiftGas

    NetGas

    GasDehydration

    ClosedDrainHdr

    Compressor

    OutletMnaifold

    CondensateHdr

  • GASDEHYDRATION GASGLYCOLEXCHANGER

  • REGENERATIONOFGLYCOL

  • PRODUCEDWATER

    TREATMENT

  • ProducedWaterConditioning ThewaterproducedalongwithOilandGasfromthewellsistobetreatedtowithin

    acceptablelevelsofqualityintermsofoilppmbeforeitisdischargedintothesea.

    ProducedWaterConditioningunitnormallyconsistsofFlashVessel,CPISeparators,IGF(inducedGasfloatationUnit)andSumpcaisson.

    FlashVesselReceiveswaterfromBothInletSeparatorsandSurgetanks.Itismaintainedat0.8kg pressure. In flash Vesselmostofthedissolvedgasesintheproducedwaterflashesout which isroutedtoLP flareheader.AssociatedOilfromtheproducedwaterintheflash vesselisroutedtocloseddrainheaderandiscollectedinthesumpcaisson.

    CPIseparatorsWaterfromtheflashvesselflowstomanyCPIseparators(corrugatedplateinterceptor)inparallel.OilfromCPISeparatoriscollectedinatankfromwhichitispumpedtooilmanifold.GasgoestoLPFlareheader.

    IGFunitWater fromCPISeparatorFlows to IGFunit. IGF isa tank inwhichgasbubblesareaeratedwithmotordrivenagitators.Thisbubblesfloattheoildropletstosurface.ThiscollectedoilispumpedtoCPIseparators.

    SumpCaissonWater from IGF is routed to Sump Caisson which is a vessel with bottom end open through which watercontinuouslydrains intothesea.Oilfloating inthesurfaceof thesumpcaisson iscollected intheblowcaissonandliftedupandflownintotheskimmerwithgasinjection.

  • PFD PRODUCEDWATERCONDITIONING

  • LPFlare

    FlashVessel

    CPISeparator

    IGF

    SumpCaisson

    ProducedWater

    SurgeTank

    ClosedDrain

    Tank

    ProducedWaterConditioning

  • Skimmer

    SumpCaisson

    BlowCaisson

    LPFlare

    OpenDrain

    FeedGas

    HotOilSupply

    SurgeTank

    Skimmer

    ClosedDrain

  • WATERINJECTION

  • WaterInjection WaterInjectionisdonetomaintainReservoirpressureaswellasWaterflooding.

    TopreventdamagetotheReservoirthequalityofwaterinjectedisstrictlycompliedwith.Also,thehealthofthepipelinescarryingtheinjectionwatertothewellsandwellplatformsistakencareofbydozingchemicalstopreventcorrosionandgenerationofH2SbySRBcolonies.

    TheMajorcomponentsofWaterInjectionsystemsare:SEAWATERLIFTPUMPSCOARSEFILTERSFINEFILTERSDEOXYGENATIONTOWERSBOOSTERSPUMPSMAININJECTIONPUMPSCHEMICALDOSINGSYSTEM

    CHEMICALDOZINGSYSTEM

    FLOCCULANTSCALEINHIBITORCORROSIONINHIBITIORCHLORINATIONBACTERICIDEOXYGENSCAVENGER

  • SEAWATERTREATMENTFORWATERINJECTION

  • SEAWATERLIFTINGANDFILTERING

    Waterfromsea isLiftedwith seawater liftpumps andfedto CoarseFiltersandfinefiltersforfiltering.

    Coarsefilterstheparticlesarefilteredto20microns Finefilterstheparticlesarefilteredupto2microns.

    Polyelectrolyteandcoagulantsareadded in seawater liftpump discharge to promote coagulation of suspendedparticles.

  • SEAWATERLIFTPUMPS

    P1010 P1020 P1030

    M M M

    M M

    FINEFILTERS

    F1170 F1180 F1190 F1200 F1210 F1220

    AIRFILTERS

    OVER BOARD

    COARSEFILTERS

    F1110 F1120 F1130CHLORINATORS

    FROMUTILITYWATERHEADER

    TOUTILITYWATERHEADER

    CH1060 CH1070

    B

    A

    C

    K

    W

    A

    S

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    I

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    E

    D

    L

    E

    V

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    POLYELECTROLYTE

    COAGULANT

    FT

    FICFICFICFICFIC

    TOFFIC

    BLOWERS

    CAPACITY:1200M3/HR

    MOTORPOWER:460KWSPEED:1500RPM

    NO.OFSATGES:2

    DISCH.PR:7.1KG/CM2

    MIN.FLOW:218M3/HR

    FILTERSUPTO20MICRONS

    INLETPR:7KG/CM2INLETTEMP:21310C

    FLOWRATE/FILTER:425.M3/HR

    FILTERSUPTO2MICRONS

    BACKWASHRATEMIN::225M3/HRMAX:450M3/HR

    DEFOAMER

    CHPRODUCTIONMIN:7.0KG/HR

    NORMAL:7.0KG/HRMAX:8.34KG/HR

    TODEOXYGENATION

    TOVACCUMPUMPS

    SEAWATERLIFTING FILTERATION

  • DEOXYGYNATIONANDPUMPING

    The filtered water flows to Deoxygenating towers for removal ofoxygen.

    Deoxygenationprevents formationofaerobicbacterialcolonies(sulfurreducing bacteria) in theWI flow lines. Vacuum pumps andOxygenscavengerchemicaldozedfacilitatesoxygenremovalinthetowers.

    Booster Pumps take suction from Deoxygenation Towers and feedMainInjectionPumps.

    Scale inhibitors, Bactericide and corrosion inhibitor chemicals aredozedinthedischargeofboosterpumps.

    MIPsdischargethetreatedwatertoWaterInjectionsubseapipelinestowellsandwellplatformsforinjectingintowaterinjectionWells.

  • MM

    M

    M

    M

    M

    M

    DEOXYGENATIONTOWERTRA

    DEOXYGENATIONTOWERTRB

    AIRFILTERS

    AIRFILTERS

    EJECTORM1420

    P1350

    P1360

    P1450

    P1460

    S

    E

    A

    L

    W

    A

    T

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    R

    S

    E

    A

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    A

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    OVERBOARD

    OVERBOARD

    OVERBOARD

    OVERBOARD

    OXYGENSCAVENGER

    OXYGENSCAVENGER

    S

    C

    A

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    E

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    N

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    O

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    R

    O

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    I

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    I

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    H

    I

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    I

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    O

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    B

    A

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    T

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    I

    I

    SE SPWI11

    P1610

    P1620

    P1630

    P1640

    P1650

    CAPACITY:415M3/HR

    MINIMUMFLOW:103M3/HRMOTORPOWER:2250KW

    SPEED:2985RPM

    MAININJECTIONPUMPS

    CAPACITY:851M3/HR

    MINIMUMFLOW:212M3/HRMOTORPOWER:322KW

    SPEED:1480RPMP:10KG/CM2

    P:134.7KG/CM2

    BOOSTERPUMPS

    P1510

    P1520

    P1530

    DEOXYGENTIONSEPARATOR

    DEOXYGENTIONSEPARATOR

    VACCUMPUMPS

    VACCUMPUMPS

    FFIC

    FIC

    FIC

    LIC

    LIC

    XSPL

    XSPL

    PIC

    PIC

    HCV

    HCV

    CAPACITY:1129.5M3/HR

    NORMAL:982.25M3/HR

    L

    1

    6

    6

    0

    L

    1

    6

    8

    0

    CAPACITY:851M3/HR

    OXYGENCONTENTOFTREATEDWATER:0.02MG/LIT

    EJECTORM1320

    AIRRATING:28.2KG/HR

    OVERBO

    ARD

    OVERBOARD

    PCV

    PCV

    DEOXYGYNATIONANDINJECTION

  • 91

    FireDetection&SuppressionSystem

    DetectionSystem

    GasDetection FusiblePlug FireDetection SmokeDetection HeatDetection

    SuppressionSystem

    FIREWATERPUMPS WaterSprinkler DryChemical FM200 CO2 Extinguisher AFFFSYSTEM

    Escape / Abandon

    Escape Ladder Scramble Net Life Ring Life Raft Life Boat Jumping Rope

  • UTILITIES POWERGENEARTION GASTURBINEDRIVENGEBERATORS WATERMAKERS ROWATERMAKERS LIVING QUARTERS AND ASSOCIATED REQUIREMNETS LIKE

    LAUNDRY,GALLEY

    EMERGENCYDIESELGENERATORS COMMUNICATIONSYSTEMS

  • SEWAGETREATMENT

  • NEWTECHNOLOGIES

    Intelligentwells

    DIGITALOILFIELD

    MULTIPHASEPUMPING

    SUBSEASEPARATIONANDREINJECTION

    GASTOWIRE

  • Gas InjectorPilot well

    Horizontalproducer

    Wells Equipped at Completion with Downhole Controls and Sensors

    Intelligent Wells

    Reservoir Saturation

    Downhole Seismic

    Flowing Phase

    Inflow Distribution

    Pressure Performance

    Continuous data from wells

    Proactive Remediation of

    Fluid Inflow

    z Remote controlled Downhole zonal control valves

    z Implement reservoir decisions without intervention

    Optical Pressure Gauge

    Optical Distributed Temperature Gauge.

    Data is transmitted up the wellbore via fibre optics.

  • Market Drivers & intelligence

    e-business

    Well Construction

    Facilities

    Export/Transport

    4D/4C - Permanent seismic

    Intelligent Wells

    Reservoir Management

    HIVE

    Integration forDecisions

    Real-time Data Transmission

    Data Store

    Control, Optimisation &

    Intervention

    Businessmodel

    Reservoirmodel

    Facilitiesmodel

    Decision DrivenAnalysis

    DIGITAL OILFIELD

    Ahighresolubledataisobtainablebya4Cseismicsurveyusing4componentsOBC(marineearthquakecable)withahydrophoneand3geophonecomponents.

  • Multiphase production systems require the transportation of a mixture of oil, water and gas, often for many miles from the producing well to a distant processing facility.

    This represents a significant departure from conventional production operations in which fluids are separated before being pumped and compressed through separate pipelines. By eliminating this equipment, the cost of a multiphase pumping facility is about 70% that of a conventional facility and significantly more savings can be realized if the need for an offshore structure is eliminated altogether.

    However, multiphase pumps do operate less efficiently (30-50%, depending on Gas volume fraction and other factors) than conventional pumps (60- 70%) and compressors (70-90%).

    Still, a number of advantages in using multiphase pumps can be realized, including: 1)Increased production through lowering backpressure on wells; 2)Elimination of vapor recovery systems; 3)Reduced permitting needs; 4)Reduction in capital equipment costs; and, 5)Reduction in footprint of operations .

    MULTI PHASE PUMPING

  • CONVENTIONAL AND MULTIPHASE PUMPING

  • z Multiphase pumping is a relatively new technology and acceptance has been hampered by a lack of engineering design tools.

    z Recently, pipeline simulation codes have incorporated the ability to model multiphase pump performance as part of the overall multiphase production system

  • Normallyusedindeepwater

    Separationofheavyoilandwater

    Reinjectionofwatertoboostproductioninamaturefielddevelopment.

    Theseparationsystemmayalsoincludescyclonemodulesthatwillperformwatertreatmentbeforereinjectionthewaterbackintothereservoir.

    SUBSEA PROCESSING

    "atruesubseadevelopmentisveryenvironmentallyfriendly."

  • THANKS

    Offshore Oil and Gas Production SystemsTHE MAJOR ELEMENTS OF OFFSHORE PRODUCTION SYSTEMWe shall discuss aboutTYPES OF OFFSHORE PLATFORMSWATER DEPTH AND TYPE OF PLATFORMOil platformsFIXED PLATFORMSFixed PlatformSemi-submersible PlatformJack-up PlatformsCompliant TowersDrillshipsFloating production systemsFPSO AND SUBSEA WELLSTension-leg platformSPAR PlatformsMaintenance and supplyCrewEssential personnelEssential personnel ONGC SystemIncidental personnelRisksEcological effectsNormally unmanned installations.WELLHEAD PLATFORMSFacilities in Well PlatformsSDPWELL CONTROL-SCHEMATICWELL CONTROLSMART WELLHEAD PLATFORMSMajor Elements of SMART platformWELLSGas Lifted wellsSELF FLOWING AND GAS LIFTED WELLSELECTRICAL SUBMERISBLE PUMPS (ESP) WELLSDIRECTIONAL WELL WELL MONITORING AND CONTROL RTU/SCADASCADA FOR WELL MONITORING, CONTROL AND PRODUCTION OPTIMIZATIONMAJOR BENEFITS OF SCADAWELL AUTOMATIONOnline Monitoring and Remote control of Injection GasREMOTE OPTIMIZATION OF WELL USING FC-MPFM SET SMART online 24 x 7 monitoring and Optimization of each well Using Gas Flow Computer- Compact GLCC Separator- Coriolis MasJack up Rig docked in a Wellhead platformPROCESSING IN OFFSHOREPROCESS PLATFORMSPROCESSESSEPARATIONGAS COMPRESSION, DEHYDRATION AND EXPORTFire Detection & Suppression System