three conditions at the p mp intake that res lt inpump ... histories... · •• plunger diameter,...

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5 th Annual Sucker Rod Pumping Workshop Workshop Wyndham Hotel, Dallas, Texas September 15 18 2009 September 15 18, 2009 Three Conditions at the P mp Intake That Res lt in Pump Intake That Result in Incomplete Pump Fillage Lynn Rowlan Lynn Rowlan

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Page 1: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

5th Annual Sucker Rod Pumping WorkshopWorkshop

Wyndham Hotel, Dallas, TexasSeptember 15 – 18 2009September 15 – 18, 2009

Three Conditions at the P mp Intake That Res lt inPump Intake That Result in Incomplete Pump Fillage

Lynn RowlanLynn Rowlan

Page 2: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Incomplete Pump FillageIncomplete Pump FillageOccurs from C to D on Pump Card Occurs from C to D on Pump Card

Steps C Steps C -- D in D in Pump OperationPump OperationSteps C Steps C -- D in D in Pump OperationPump OperationPump OperationPump Operation

Pump is a Pump is a CompressorCompressor

Pump OperationPump Operation

Pump is a Pump is a CompressorCompressor

BB CCCompressorCompressorCompressorCompressor at [C] Pb = Pintk

at [D] Pb = PdisPDisPDis -- Discharge PressureDischarge PressureAA DD

at [D] Pb PdisggPB PB -- Pressure in BarrelPressure in BarrelPintkPintk -- Intake PressureIntake Pressure

C)C) Standing Valve closes, when plunger reaches Standing Valve closes, when plunger reaches top of stroke, rods start to untop of stroke, rods start to un--stretch to stretch to transfer fluid load, transfer fluid load, FoFo, from rods [C] onto , from rods [C] onto tubing [D].tubing [D].

CC--D) Plunger applies D) Plunger applies pressure to fluids pressure to fluids inside pump barrelinside pump barrelg [ ]g [ ]

D) D) Standing valve Opens when pressure in Standing valve Opens when pressure in pump barrel >= Pump Discharge Pressure, pump barrel >= Pump Discharge Pressure, PDisPDis. .

inside pump barrel, inside pump barrel, to compress fluids to compress fluids in Pump barrel and in Pump barrel and increase pressure.increase pressure.

Page 3: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Incomplete Pump Fillage1.1. Fluid PoundFluid Pound -- Not enough Not enough

liquid to fill the pump barrel: liquid to fill the pump barrel: ll i fl l thll i fl l th

CCwell inflow less than pump well inflow less than pump displacement, pumped off.displacement, pumped off. CompressionCompression

DD

2.2. Gas InterferenceGas Interference -- Both gas Both gas and liquid at pump intake and liquid at pump intake

fill b lfill b lpressure fill pump barrel pressure fill pump barrel during the upstroke.during the upstroke.

DD

CC

CompressionCompression

3.3. Flow into pump intake Flow into pump intake chokedchoked -- flow through SV is flow through SV is

l th ll th l

DD

CCzero or less than plunger zero or less than plunger displacement.displacement. DD Collision?Collision?

Page 4: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Transfer Fluid Load from C to D Transfer Fluid Load from C to D from Rods to Tubingfrom Rods to Tubing

@ [C] Fo = Fluid Load@ [C] Fo = Fluid LoadPb Pi tkPb Pi tk

At [C] SVAt [C] SVBall SeatsBall Seats

BB

Pb = PintkPb = Pintk(Pdis(Pdis--Pintk)*Area PumpPintk)*Area Pump

Ball Seats Ball Seats Pdis > Pb Pdis > Pb Pb = PintkPb = Pintk

BBCC

at [C] Pb = PintkPlunger Plunger

AA DD

Stroke Stroke LengthLength at [D] Pb = Pdis

@ [D] TV Opens@ [D] TV OpensFo = 0Fo = 0

At [D] TVAt [D] TVOpensOpens

Pb = PdisPb = Pdis(Pdis(Pdis--Pdis)*Area PumpPdis)*Area Pump

Opens Opens Pdis = Pb Pdis = Pb Pb > PintkPb > Pintk

Page 5: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Calculated Pump Card Loads:Calculated Pump Card Loads:

Pump Card Rests on Zero Load Line on Down Stroke. Pump Card Rests on Zero Load Line on Down Stroke. Pump Card Near Fo From Fluid Level on Up Stroke. Pump Card Near Fo From Fluid Level on Up Stroke.

20.00

22.50

Wrf + Fo Max

Calculated Pump Card Loads:Calculated Pump Card Loads:SV Open Upstroke: SV Open Upstroke:

FoFo Max = (Max = (PdisPdis –– 0)*Ap0)*ApFF ((PdiPdi Pi tkPi tk)*A)*A

Surface Card

15.00

17.50 FoFo = (= (PdisPdis -- PintkPintk)*Ap)*ApTV Open TV Open DownstrokeDownstroke: :

FoFo = 0= 0

10.00

12.50

Fo Max

Wrf

Pump Card Reference Lines:Pump Card Reference Lines:1.1. FoFo MaxMax -- assumes pump intake assumes pump intake

pressure is zero, where well pressure is zero, where well provides no help in lifting the fluidprovides no help in lifting the fluid

5.00

7.50 Fo From Fluid Levelprovides no help in lifting the fluid provides no help in lifting the fluid to the surface.to the surface.

2.2. FoFo From Fluid LevelFrom Fluid Level -- assumes assumes pump intake pressure determined pump intake pressure determined from fluid level shot, where well’s from fluid level shot, where well’s PIP id h l i lifti thPIP id h l i lifti th

Well

Fo ~ Height of Pump Card

0

2.50

156.0

PIP provides help in lifting the PIP provides help in lifting the fluid.fluid.

3.3. Zero Load LineZero Load Line –– assumes assumes pressure above and below the pressure above and below the plunger are equal; no friction dueplunger are equal; no friction due

Fluid Load Lifted by RodsFo ~ Height of Pump Card

0 168.0-2.50plunger are equal; no friction due plunger are equal; no friction due to fluid displacing through SV on to fluid displacing through SV on down strokedown stroke

Pump Card

Fo loads measured Dynamometer or calculated From Fluid Level.Fo loads measured Dynamometer or calculated From Fluid Level.

Page 6: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Incomplete Pump Fillage

1.1. Fluid PoundFluid Pound –– Rod Loading Rod Loading Fo = FoFo = Foggis Fomax, Pintk is low, Pb = is Fomax, Pintk is low, Pb = Pintk.Pintk.

Fo = FoFo = Fomaxmax

Fo Fo flfl = Fo= Fomaxmax

2.2. Gas InterferenceGas Interference -- Rod Rod Loading is Fo fl Pintk isLoading is Fo fl Pintk is

Fo < FoFo < FomaxmaxFo Fo flfl = Fo= Fo

Loading is Fo fl, Pintk is Loading is Fo fl, Pintk is high, Pb = Pintk.high, Pb = Pintk.

Fo Fo flfl < Fo< Fomaxmax

3.3. Flow into pump intake Flow into pump intake chokedchoked -- Rod Loading is Rod Loading is Fo = FoFo = Fomaxmax

Fomax, Pintk is high, Pb = Fomax, Pintk is high, Pb = Zero (0); much << Pintk.Zero (0); much << Pintk. Fo Fo flfl < Fo< Fomaxmax

Page 7: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Synthetic Pump Cards:Synthetic Pump Cards:Fluid Pound ~ PIP is LowFluid Pound ~ PIP is LowSynthetic Pump Cards:Synthetic Pump Cards:Fluid Pound ~ PIP is LowFluid Pound ~ PIP is Low

Tubing anchored, EPT<MPT.Tubing anchored, EPT<MPT. Unanchored tubing, EPT<MPTUnanchored tubing, EPT<MPTTubing anchored, EPT MPT.Tubing anchored, EPT MPT. Unanchored tubing, EPT MPTUnanchored tubing, EPT MPT

Fo Fluid LevelFo MaxFo Up

Fluid pound Fluid pound -- well being pumped off. Pump components are well being pumped off. Pump components are functioning properly. BUT, sudden unloading of rods results in functioning properly. BUT, sudden unloading of rods results in rod buckling and reduced equipment life! Shoot fluid level torod buckling and reduced equipment life! Shoot fluid level torod buckling and reduced equipment life! Shoot fluid level to rod buckling and reduced equipment life! Shoot fluid level to verify pump intake not blocked and fluid level at pump intake.verify pump intake not blocked and fluid level at pump intake.

Page 8: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Control Run Time When Control Run Time When Pump Displacement Exceeds Inflow From WellPump Displacement Exceeds Inflow From Well

Same Well with Full PumpSame Well with Full PumpO TV l h P F llO TV l h P F ll

p pp p

Open TV only when Pump FullOpen TV only when Pump Full

Pump Capacity Exceeds Pump Capacity Exceeds I fl f Fl id f W llI fl f Fl id f W ll

Full

Inflow of Fluids from WellInflow of Fluids from Well..

Full

Controlling Pump Run TimeControlling Pump Run TimeImproves Efficiency, Reduces Improves Efficiency, Reduces

Pound Shock Loads, and Reduces Shock Loads, and Reduces FailuresFailures..

Page 9: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Fluid PoundFluid Pound -- Fluid Level @ PumpFluid Level @ PumpTimer or Pump Off Controller CandidateTimer or Pump Off Controller CandidateFluid PoundFluid Pound -- Fluid Level @ PumpFluid Level @ PumpTimer or Pump Off Controller CandidateTimer or Pump Off Controller Candidate

Fl id L lFl id L lFluid Level Fluid Level @ Pump@ PumpFo Pump @ Fo MaxFo Pump @ Fo Max

Fluid Fluid PoundPound

Page 10: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Synthetic Pump Cards:Gas InterferenceSynthetic Pump Cards:Gas Interference

Tubing anchored, EPT<MPT.Tubing anchored, EPT<MPT. Unanchored tubing, EPT<MPTUnanchored tubing, EPT<MPTFF MMg ,g , Unanchored tubing, EPT MPTUnanchored tubing, EPT MPT

Fo Fluid LevelFo Fluid Level

FoFo MaxMax

GasGas InterferenceInterference isis causingcausing decreasedecrease ofof EPTEPT.. PumpPump componentscomponents arearefunctioningfunctioning properlyproperly.. UsuallyUsually unstableunstable pumppump fillagefillage andand EPTEPTchangeschanges fromfrom strokestroke--toto--strokestroke.. WhenWhen gasgas interferenceinterference isis presentpresentexpectexpect increasedincreased rodrod--onon--tubingtubing wearwear duedue toto rodrod bucklingbucklingcompressingcompressing gasgas inin pumppump barrelbarrel..

Page 11: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Gas Interference: Incomplete Pump Fillage and High Fluid LevelGas Interference: Incomplete Pump Fillage and High Fluid Level

Fluid Level Fluid Level Above PumpAbove Pump

Fo Well

pp

Fo Rods

Fo Pump < Fo MaxFo Pump < Fo MaxFo Pump < Fo MaxFo Pump < Fo Max

Page 12: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Synthetic Pump Cards:Synthetic Pump Cards:Severe Fluid Pound Severe Fluid Pound –– Blocked Pump IntakeBlocked Pump IntakeSynthetic Pump Cards:Synthetic Pump Cards:Severe Fluid Pound Severe Fluid Pound –– Blocked Pump IntakeBlocked Pump Intakepppp

Tubing anchored, EPT<MPT.Tubing anchored, EPT<MPT. Unanchored tubing, EPT<MPTUnanchored tubing, EPT<MPTTubing anchored, EPT MPT.Tubing anchored, EPT MPT. Unanchored tubing, EPT MPTUnanchored tubing, EPT MPT

Fo Fluid LevelFo Fluid Level

Fo MaxFo MaxFo UpFo Up

Fo Fluid LevelFo Fluid Level

Severe fluid pound, usually occurs when the intake into the pump is Severe fluid pound, usually occurs when the intake into the pump is completely blocked off. Strainer nipple, pump intake below fill, completely blocked off. Strainer nipple, pump intake below fill, standing valve stuck shut can starve pump. Stuffing box leak and standing valve stuck shut can starve pump. Stuffing box leak and reduced equipment life result! Shoot fluid level to verify pump intake reduced equipment life result! Shoot fluid level to verify pump intake is blocked and fluid level above pump intakeis blocked and fluid level above pump intake

Page 13: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Severe Fluid Pound: Flow into Pump ChokedFluid Pound and High Fluid LevelSevere Fluid Pound: Flow into Pump ChokedFluid Pound and High Fluid Level

Fluid Level Fluid Level Above PumpAbove PumpAbove PumpAbove Pump

Fo WellFo Well

Fo Pump = Fo MaxFo Pump = Fo Max

Fo RodsFo Rods

Page 14: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Gas Compressionp

Traveling valve Traveling valve opens whenopens whenopens when opens when pressure in barrel pressure in barrel exceeds the exceeds the pressure at thepressure at theThe dynamometer card pressure at the pressure at the pump discharge pump discharge at the bottom of at the bottom of the tubing.the tubing.

indicates gas in the pump. Gas compression occurs during the downstroke ggduring the downstroke from C to D and causes the traveling valve to opened at D.

Page 15: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Effect of PIP onGas Interference and Fluid PoundEffect of PIP onGas Interference and Fluid Pound

GasGas

PV PVPV PV((----------) = () = (------------))

Z ZZ Z

IntakeIntake

Z ZZ ZIntake DischargeIntake Discharge

LiquidLiquid

IsoIso--thermalthermalNo Change in RsNo Change in Rs

LiquidLiquidDischargeDischarge

Page 16: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Effect of PIP on Fillage of Pump CardEffect of PIP on Fillage of Pump Card

Gas Free PumpGas Free Pump

GasGas

Gas Free Pump Gas Free Pump Fillage LineFillage Line

GasGasGas Free Pump Fillage = 50%Gas Free Pump Fillage = 50%

@ 10 Psi@ 10 Psi

Total Gas Fillage = 50%Total Gas Fillage = 50%

@ 0 s@ 0 sEff Plunger Stroke = 47”Eff Plunger Stroke = 47”EPS Fillage = 52%EPS Fillage = 52%Gas Fillage [D] = 2%Gas Fillage [D] = 2%

@ 500 P i@ 500 P i

LiquidLiquid

@ 500 Psi@ 500 PsiEff Plunger Stroke = 60”Eff Plunger Stroke = 60”EPS Fillage = 66.7%EPS Fillage = 66.7%Gas Fillage [D] = 16 7%Gas Fillage [D] = 16 7%LiquidLiquid Gas Fillage [D] = 16.7%Gas Fillage [D] = 16.7%

Page 17: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Rods Buckle (Train Wreck Effect)Pump Load & Velocity

Plunger Slows to Open TV

GasGasGas Gas InterferenceInterference

Page 18: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Rods Buckle (Train Wreck Effect )Pump Load & Velocity

Plunger Slows to Open TV

Plunger Slows to Open TV

Fluid PoundFluid Pound

Page 19: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Gas Compression and Train Wreck EffectGas Compression and Train Wreck Effect

1.1. Gas Compression occurs when the pump barrel is Gas Compression occurs when the pump barrel is partially/filled with gas.partially/filled with gas.partially/filled with gas.partially/filled with gas.

2.2. Sudden opening of TV reduce equipment lifeSudden opening of TV reduce equipment lifea.a. Is it uphole compression whacking rods against the tubingIs it uphole compression whacking rods against the tubinga.a. Is it uphole compression whacking rods against the tubingIs it uphole compression whacking rods against the tubingb.b. Pin failures due to rod slap loosening the couplingsPin failures due to rod slap loosening the couplings

3.3. Rod buckling up the hole occurs when the pump slows Rod buckling up the hole occurs when the pump slows ggdown to compress the gas and liquid in the pumpdown to compress the gas and liquid in the pump

4.4. Rods must apply a force to increase the pressure Rods must apply a force to increase the pressure i id th b l t t th th di hi id th b l t t th th di hinside the barrel to greater than the discharge inside the barrel to greater than the discharge pressure. pressure.

55 Rods above the pump go into compression and buckleRods above the pump go into compression and buckle5.5. Rods above the pump go into compression and buckle Rods above the pump go into compression and buckle when the pump velocity decreases in order to increase when the pump velocity decreases in order to increase the pressure inside the pump.the pressure inside the pump.

Page 20: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Fluid Pound and Rod BucklingFluid Pound and Rod Buckling

1.1. Fluid Pound may not be Exactly Correct TermFluid Pound may not be Exactly Correct Terma.a. Occurs with incomplete pump fillage at low pump intakeOccurs with incomplete pump fillage at low pump intakea.a. Occurs with incomplete pump fillage at low pump intake Occurs with incomplete pump fillage at low pump intake

pressure pressure b.b. Forces at pump may not cause trouble Forces at pump may not cause trouble c.c. UpUp--hole rod compression and rod on tubing wear is the likely hole rod compression and rod on tubing wear is the likely

problem problem

2.2. Low Pressure Gas in the pump causes fluid poundLow Pressure Gas in the pump causes fluid poundp p pp p pa.a. Pump stops just as bad if the gas is in the 100Pump stops just as bad if the gas is in the 100--200 psi range, 200 psi range, b.b. Rod on tubing wear can be worse at higher intake pressuresRod on tubing wear can be worse at higher intake pressures

3.3. Traveling valve opens when pressure in barrel exceeds Traveling valve opens when pressure in barrel exceeds discharge pressure at the bottom of the tubing.discharge pressure at the bottom of the tubing.a.a. TV always opens before hitting fluid (except blocked intake)TV always opens before hitting fluid (except blocked intake)b.b. Plunger maybe a 1/16th inch away when "fluid pound“ occursPlunger maybe a 1/16th inch away when "fluid pound“ occurs

Page 21: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Rods Buckle (Collision with Liquid )

20.00

22.50

Wrf + Fo Max

15.00

17.50

Wrf

Wrf Fo Max

Pump Load 0 &

10.00

12.50

Pump Load 0 & Velocity -11 ft/sec

5 00

7.50

10.00

Plunger Stops After TV Opens

Gas Compression Does Not Slows Plunger to Open TV

2.50

5.00 Fo Max

Fo From Fluid Level

Blocked IntakeBlocked Intake

Plunger to Open TV

0 120.0-2.50

0 106.7Blocked IntakeBlocked IntakeNegative Effective Load

Page 22: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

0 BBLS in Tank ~ Pump Disp 26.9 BPD

Slippage Between Plunge/Barrel Fills PumpSlippage Between Plunge/Barrel Fills Pump0 BBLS in Tank Pump Disp 26.9 BPD

CC

EmptyEmpty

D

Plunger Velocity -11 to -5 in/sec

Blocked IntakeBlocked Intake

Page 23: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Pump Fillage Due to Only SlippagePump Fillage Due to Only Slippage

25 BPD 25 BPD Pump Pump FillageFillageFillageFillage

23” 23”

Blocked IntakeBlocked Intake

Page 24: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Incomplete Pump FillageIncomplete Pump Fillage1) Fo, Pump Load location w/ respect to Zero, Fo

From Fluid Level and Fo Max Load Lines areFrom Fluid Level, and Fo Max Load Lines are Used to Identify Incomplete Pump Fillage.

2) Fluid Pound and Blocked Intake Pump cards look ) psimilar except that:• Fluid Pound – Fluid level at Pump

Bl k d I k Fl id L l Hi h b P• Blocked Intake – Fluid Level High above Pump3) Fluid Pound and Gas Interference both have gas

in the pump that must be compressed from [C D]in the pump that must be compressed from [C-D]4) When the Intake is Blocked, then no gas is in the

pump barrel and Plunger “Pounds” the Fluid insidepump barrel and Plunger Pounds the Fluid inside the Pump Barrel.

5) Negative Load seen when Plunger HitsHits Liquid

Page 25: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Data Requirements Data Requirements -- PFLPFLqq•• Requires stabilized conditionsRequires stabilized conditions

•• Determination of Liquid Level DepthDetermination of Liquid Level Depth–– Avg. Joint Length, Acoustic Velocity, SG Gas ….Avg. Joint Length, Acoustic Velocity, SG Gas ….g g yg g y

•• Measurement of casing pressureMeasurement of casing pressure

•• Tubing Casing Size & TVD Pump DepthTubing Casing Size & TVD Pump Depth•• Tubing, Casing Size, & TVD Pump DepthTubing, Casing Size, & TVD Pump Depth

•• Oil, water and annular gas densitiesOil, water and annular gas densities

•• Measurement of casing pressure buildup rate Measurement of casing pressure buildup rate (at Producing Conditions)(at Producing Conditions)

Sept. 15 - 18, 2009 2009 Sucker Rod Pumping Workshop 25

Page 26: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Data Requirements Data Requirements -- DynoDyno•• Requires stabilized conditionsRequires stabilized conditions

M t f t biM t f t bi

•• Requires stabilized conditionsRequires stabilized conditions

M t f t biM t f t bi

qq yy

•• Measurement of tubing pressureMeasurement of tubing pressure

•• True Vertical Pump DepthTrue Vertical Pump Depth

•• Measurement of tubing pressureMeasurement of tubing pressure

•• True Vertical Pump DepthTrue Vertical Pump Depth

•• Oil, water and gas densitiesOil, water and gas densities

•• Oil water and gas Production RateOil water and gas Production Rate

•• Oil, water and gas densitiesOil, water and gas densities

•• Oil water and gas Production RateOil water and gas Production RateOil, water, and gas Production RateOil, water, and gas Production Rate

•• Tubing Fluid GradientTubing Fluid Gradient

Oil, water, and gas Production RateOil, water, and gas Production Rate

•• Tubing Fluid GradientTubing Fluid Gradient

•• Plunger Diameter, Rod String Plunger Diameter, Rod String

•• Damping CoefficientsDamping Coefficients

•• Plunger Diameter, Rod String Plunger Diameter, Rod String

•• Damping CoefficientsDamping Coefficients

Page 27: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

Copyrightpy g

Rights to this presentation are owned by the company(ies) and/or author(s) listed on the title page By submitting this presentation toauthor(s) listed on the title page. By submitting this presentation to the Sucker Rod Pumping Workshop, they grant to the Workshop, the Artificial Lift Research and Development Council (ALRDC), and the Southwestern Petroleum Short Course (SWPSC), rights to:

– Display the presentation at the Workshop.– Place it on the www.alrdc.com web site, with access to the site to be as

directed by the Workshop Steering Committee.Pl it CD f di t ib ti d/ l di t d b th W k h– Place it on a CD for distribution and/or sale as directed by the Workshop Steering Committee.

Other use of this presentation is prohibited without the expressed written permission of the author(s). The owner company(ies) and/orwritten permission of the author(s). The owner company(ies) and/or author(s) may publish this material in other journals or magazines if they refer to the Sucker Rod Pumping Workshop where it was first presented.

Sept. 15 - 18, 2009 2009 Sucker Rod Pumping Workshop 27

Page 28: Three Conditions at the P mp Intake That Res lt inPump ... Histories... · •• Plunger Diameter, Rod String Plunger Diameter, Rod String •• Damping Coefficients Damping Coefficients

DisclaimerThe following disclaimer shall be included as the last page of a Technical Presentation or Continuing Education Course. A similar disclaimer is included on the front page of the Sucker Rod Pumping Web Site.gThe Artificial Lift Research and Development Council and its officers and trustees, and the Sucker Rod Pumping Workshop Steering Committee members, and their supporting organizations and companies (here-in-after referred to as the Sponsoring Organizations), and the author(s) of this Technical Presentation or Continuing Education Training Course and their company(ies), provide this presentation and/or training material at the Sucker Rod Pumping Workshop "as is" without any g g ywarranty of any kind, express or implied, as to the accuracy of the information or the products or services referred to by any presenter (in so far as such warranties may be excluded under any relevant law) and these members and their companies will not be liable for unlawful actions and any losses or damage that may result from use of any presentation as a consequence of any inaccuracies in, or any omission from, the information which therein may be contained.The views, opinions, and conclusions expressed in these presentations and/or training materials are those of the author and not necessarily those of the Sponsoring Organizations. The author is solely responsible for the content of the materials.The Sponsoring Organizations cannot and do not warrant the accuracy of these documents beyond the source documents, although we do make every attempt to work from authoritative sources. g y pThe Sponsoring Organizations provide these presentations and/or training materials as a service. The Sponsoring Organizations make no representations or warranties, express or implied, with respect to the presentations and/or training materials, or any part thereof, including any warrantees of title, non-infringement of copyright or patent rights of others, merchantability, or fitness or suitability for any purpose.

Sept. 15 - 18, 2009 2009 Sucker Rod Pumping Workshop 28