Gohfer-培训英文课件8-proppant-transport.pptx
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- Gohfer 培训 英文 课件 proppant transport
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1、ProppantTransport&ScreenoutBehaviorR.D.Barree2009Inthissession Lookattraditionalproppanttransportanditsassumptions Lookatcommonremediesforearlyscreenout Whatfactorsactuallyaffectproppanttransport?2009ProppantTransport&Settling Simplemodelsassume1Dflowandmodelsingleparticlesettling(StokesLaw) Fluidan
2、dparticlevelocityprofilesaremuchmorecomplexin3Dflow. Slurrydensitygradientscausegravityunderrunning,fluidshear,andnonhomogeneousconcentrationprofiles. Fluidpropertiesandleakoffcausetransverseparticlemigration LateralparticlemotionchangestransportandleadstoscreenoutTraditionalPropTransportFrac height
3、(assumed to beconstant)Suspended proppant slurry(uniform concentration)Clean pad fluid tocreate w=3-6xdFracture half-lengthSettled sand bank20092009CommonAssumptions:FluidLoss/Transport/Screenout Proppantishomogeneouslydistributed Vertically,laterally,transverselySandandfluidtraveltogetherPadisrequi
4、redtoopenwidthforsandPadisdepletedbyleakoffScreenoutscausedbypropbridgingPropconcentrationincreasedbyleakoffFalseassumptionsleadtofailedremediesCommonRemediesforEarlyScreenout(Ifcausedbypaddepletionandbridging)PumpmorepadvolumeIncreasepumprateUsehigherviscosityfluidsUsesmallerproppantsUsefluidlossad
5、ditivesSometimes they work, and sometimes NOT!20092009FactorsAffectingProppantTransport Particlevelocityprofileinfracture Concentrationdistributionacrossfracturewidth Slurryviscosityincreasewithsolidsaddition Singleparticle“Stokes”settlingvelocity “Hindered”particlesettling Convectionfromslurrybulkd
6、ensitygradients Proppantholdup ProppantbridgingCum. Particle Count200910.80.60.40.20VelocityDistributionofParticlesBetweenParallelPlates1.20123456Particle Velocity, cm/secFor a uniform particledistribution, the velocityprofile is given by thecumulative frequencyplot.Cum. Particle Count20090.80.60.40
7、.20ParticleVelocityProfilesNormalizedtoFluidVelocity1.2100.20.40.60.811.21.41.6Relative Particle VelocityCv=0%Cv=10%Cv=25%Cv=35%Cv=55%Velocity, cm/secProppantnotHomogeneouslyDistributed654321000.20.40.60.81Normalized Slot Width2009Particles at highconcentrationParticles at lowconcentration2009Single
8、ParticleSettlingVelocityPredictions Terminalsettlingvelocityforasingleparticleinaninfinitefluidbody: StokesLawforlaminarflow AllensEquationfortransitionflow NewtonsEquationforturbulentflow Terminalvelocitycanbemodifiedformultipleparticleinteractions. Walleffectscanbeconsideredfornarrowchannels.( )vt
9、 =1.74d g(s l) 2009SingleParticleTerminalSettlingVelocitiesStokes laminarflowregime18Allen transitionflowregime0.721.180.20d(g(s l) l)0.45lvt =0.5Newton turbulentflowregime0.5 l Settling Velocity, cm/sec20090.10.010.0010.11Particle Diameter, inchesSingleParticleSettlingRatesina1.0cpNewtonianFluid100
10、101StokesAllenNewtonActual1000.011250 40 30 20Mesh SizeSettling Velocity, cm/sec2009SingleParticleSettlingRatesina55.0cpNewtonianFluid1001010.10.010.0010.11Particle Diameter, inchesStokesAllenNewtonActual1000.011250 40 30 20Mesh Size2009SlurrySettlingExperimentsinaVerticalSlotModel Parallelplatemode
11、l5feetx6inchesx0.25inches 30%and40%PEGsolutions 30/50meshand95meshsilicasandslurries Volumetricconcentrationsfrom055%solids SlurrysettlingvelocitycomparedtoStokesvelocitySettling Velocity, cm/sec2009Solids Concentration, Cv10.1SlurrySettlingRatesControlledbyBulkDensityGradients1001000.10.20.30.40.5V
12、meas(95)Vmeas(40)Stokes(40)Stokes(100)Vcalc0.010.001( ) P g gh f c f + wa 12vs =2009ProppantMovementbyBulkFlowor“Convection” ConvectionPhys:”Transmissionofenergyormassbyamediuminvolvingmovementofthemediumitself.” McGrawHillDictionaryofScientificandTechnicalTerms,FourthEditionz2For fluid flow between
13、 parallel plates.2009ThinFluidTransportisDifferentFromSuspensionTransportProppant drops out of fluid quickly. All solid transportis in a thin “traction carpet”.Bank height builds to an equilibrium based on fluidvelocity. A clear fluid layer is maintained above thesettled bank. The bank advances by “
14、dune building”.2009Video ofSlickWaterSandTransport2009ProppantBridgingandScreenouts Proppantparticlesbridgeinacircularorifice36xtheparticlediameter ParticlesbridgeinaslotwhenthegapequalsthelargestparticlediameterStable BridgeUnstable-FlowDismantles BridgePVariableSlot WidthViewing direction in video
15、2009Slurry Inlet4-12 ppaSlurryOutletFracture ChannelWidth = 0.3”VariableWidthSlotApparatusModel Width=18”SlotBridgingVideoFlowislefttorightBoratexlinkedGuarfluid8ppa20/40OttawasandslurryBlack16/30ceramicmarkersSlotwidthequalsmaximum(16mesh)particlediameter20092009ProppantBridgingVideoCopyright B&A20
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