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AcidizingThe Fundamentals
Damage Assessment
Workover & Completion CommonalitiesFluid is put into the wellbore and/or formation
Tubulars of some sort are run into the well
Fundamental Acid TechniquesWellbore clean-up (tubing/casing)Matrix acidizing (sandstone or carbonates)Acid fracturing (carbonates)
Types of AcidMineralHydrochloric - HClHydrochloric/Hydrofluoric - HCl/HFOrganic (slower reacting less corrosive)AceticFormicPowdered (acid sticks)SulfamicChloroacetic
Dissolving Capability15% HCL 1.84 ppg28% HCL 3.68 ppg9:1 mix 7.5% HCL : Acetic 1.64 ppg9:1 mix 15% HCL : Acetic 2.48 ppg9:1 mix 28% HCL : Acetic 3.72 ppg10% Acetic 0.71 ppg
Acid Reaction Rate
Basic Equation
2HCl + CaCO3 H2O + CO2 +CaCl2 Water Salt Gas1000 1843 1040 6620 2050Gals lbs gals ft3 lbs
Controlling FactorsPressureLess than 500 psiTemperatureAdd 20, double reaction rateSubtract 20, half the reaction rateVelocityAccelerate the mass transferFlow patterns radial, linear, cylindrical
Controlling FactorsConcentrationStronger is faster (to a point)Contact area & volume ratioMatrix = large surface area (30000:1)20% limestone with 10 mdNatural fracture (3000:1)Same limestone with a 0.001 natural fractureFracture = smaller surface area (32:1)Same limestone with a 0.1 created fracture
Controlling FactorsFormation compositionSurface wettingViscosity
Retarded AcidsGelled acidMineral/organic mixCommon ion
Basic Equation
2HCl + CaCO3 H2O + CO2 +CaCl2
Retarded AcidsGelled acidMineral/organic mixCommon ionOil-wet barriersEmulsionsHigh concentrations
Acid additivesCorrosion Inhibitors specify time and temperatureSurface Active Agents anionic, cationic, nonionic, amphotericAnionic tend to water wet sand, emulsify oil in water, break water in oil emulsions, disperse claysCationic tend to water wet carbonates, emulsify water in oil, break oil in water emulsions, flocculates clayAnionic and cationic surfactants mix like matter and anti-matterNonionic tends to be the most popular surfactants
Acid Additives (cont)Non-emulsifiers (acid and oil)Chemical retarders (carbonates only)Foamers2 gpt < 75 F3 gpt < 130 F5 gpt < 200 F7 gpt < 250 F10 gpt < 300 F13 gpt < 350 F
Acid Additives (cont)Alcohol (dry gas wells)Methanol < 200 FEthanol < 300 FMutual solvents (need?)Anti-sludge agents (asphaltic crudes 5-20 gpt)Clay stabilizers
Acid Additives (cont)Iron sequestering agentsIron in tubulars, scale and fomation mineralsMost treatments minimum control of 1000 mpl requires 10-15 ppt sodium erythorbateControl severe iron concerns 5000 mpl60 to 120 - 1% acetic + 50 ppt citric120 to 180 - 2% acetic + 100 ppt citric or 50-65 ppt sodium erythorbate180 plus 50-65 ppt sodium erythorbate
Acid Additives (cont)Friction reducersGelling agentsFluid loss additivesDiverting materialRock saltWax beadsOil soluble resinsBenzoic acid flakes (story time)
Wellbore Clean-upClean-upMill scaleCorrosion scalePipe dopePickled tubing
The Pickle JobMinimum volume of aromatic solvent 250 gallonsScale basis 0.1 lb/ft in 5 20# casing (or 0.003 of 5.0 sg magnetite mill scale)400 gal/1000 5 100 gal/1000 2 7/8
The Pickle Job15% HClMinimum CIAromatic solvent pre-flushNo iron control
Catch return samples
Matrix AcidizingBelow fracture gradientWormholesSize?Length?Number?
WormholesFluid loss rate determines length, inches to feet longFluid loss additivesViscosityNot a function of reaction rate!
28% HCl
Sandstone Matrix AcidizingHCl for mud damage removalCarbonate FLADehydrate bentonite clayHCl/HF for stimulation (sandstone only!)Always at matrix ratePermeability dominatesShallow stimulation
HCl/HF AcidizingAlways need HCl pre-flushHF reacts more quickly with clays than silicaDont use sodium, potassium or calcium salt waters for flushFeldspar means use half strength (13.5%:1.5%)Flush with ammonium chloride or HCl spacer
Acid Fracturing (Carbonates)Factors affecting penetrationFluid lossInjection rateFracture widthFactors affecting conductivityHeterogeneityClosure pressureRock strength
Acid Fracturing MethodsDensity controlledViscous fingering Foamed acidOverbalanced surge
Density Control
Density Control
Viscous Fingering Acid
Overbalanced SurgingPlacement of unconventionally small volumes of acid in a fracture mode is not possible in a conventional mode.
Overbalanced SurgingPlacement of acid is possible with overbalanced surging even with large variances in permeability
Carbonate Acidizing
Reasons for Carbonate Acidizing
Damaged permeabilityLow permeabilityLow perforation efficiency
Matrix Treatment DesignDetermine fracture gradientCalculate maximum BHTPCalculate maximum allowable STPEstimate injection rate - Darcy radialDetermine acid volume 50-200 gal/ftSpecify acid type, volume, rate and max pressure
Fracture AcidizingMajority of carbonate reservoir treatments are acid fracsGood conductivity is the key to successful stimulationProductivity increases of 2.5-13 fold
Factors Affecting Fracture GeometryInjection rate
Fluid viscosity
Fluid volume injected
Fluid lossRock properties
Formation fluids
Formation stresses
Reaction rates
Rule of Thumb for Acid VolumeFill the fracture with an acid volume of regular 15% HCl that is three times (3X) the fracture volume to be etched.
Treatment DesignOptimize the treatmentFracturing calculationsRock compositionClosed fracture acidizing (10-20%)Treatment review
General volumesAcid wash/soak 10-25 gals/ftMatrix acid 100-200 gals/ftAcid Fracture 400-600 gals/ft
Questions???
Pat H. Sanderson 1-13 #1Stimulation EvaluationA Look Back and Forward byPat Handren
Prior Stimulation ModelOriginal perforations16,760 16,83085/15 split dolomite/limestone10,000 gals 15% HClBHT - 277FProblemsNo cooldownReaction time ~2 min.Small radius of penetration (50-100)
PositivesReservoir has potential!
Pat H. Sanderson 1-13 #1Condensate History Match
Chart1
54022500
4562.55300
40884400
3724.19630672774000
3619.29583061743600
3520.14298143453250
3426.27797583773230
3337.28879747063230
3252.80515084223200
3172.49331088073050
3096.05171709162900
3042.10121762113000
3025.70457164633000
3009.48373092712700
2993.43588305813000
50-60' acid frac
Production Data
Year
BOPM
Pat Sanderson 1-13 #1History Match on Condensate
Sheet1
years50-60' acid frac300' acid frac300' prop fracProduction Data
0.2540210181117391482793222500600068
0.44563886610004125243274530018720145
0.6408878518715112215239440029280121
0.8372473698093102202222400038880110
13619703476569919321036004752099
1.23520672772659618419932505532089
1.43426644669119417718932306307288
1.63337618865909117018132307082488
1.83253607864568916717732007850488
23172598263408716417430508582484
2.23096589062288516117129009278479
2.43042579961208315916830009998482
2.630265712601683156165300010718482
2.830095627591582154162270011366474
329935545581782152159300012086482
Sheet2
Perforations
TopBottomnetgrossDolomiteCalcite
1660416620168812
16637166425385545
167401674666337
1676016782227525
168061683024908812
73128
Average79.767123287720.2328767123
Height700.0033874529
Length429.717341482pp -30200008-1055.25951861712320.8997819184
Width0.0166666667p - 3050008-10
Efficiency0.520%200008-10
500 bs1000
Volume15000pp15000
Reaction Time41p5000
Rate8.710801393720%15000
f6000
870005200035000
Sheet3
Acid Volume
Acid Strength
Relative Reaction Rates
Keys to Successful AcidizingCool down the reservoir Increase the fracture widthRate dependent on pressureMaximize penetration distanceClosed fracture acidizingOverflush
Two Staged Acid ProposalFirst stage20,000 gals 30# gel5,000 gals 30# borate x-linked20,000 gals 20% HCLPump at 8-10 BPM, but use pressure to dictate maximum rateDivert with 500 bioballsSecond stage15,000 gals 30# gel5,000 gals 30# borate x-linked15,000 gals 20% HCLReduce rate & over flush
Fracture ProposalRemove tubing from well.Fracture stimulate down casing @ 30 BPM using a 35# borate x-linked system and 224,000# 20/40 bauxite in 2-5ppg stages.Lubricate packer.Rerun tubing.
Cost EstimatesAcidizingBook Price - $90,000 Discounted @ 40% - $54,000
FracturingBook Price - $375,000Discounted @ 40% - $225,000 (4:1 cost ratio)
Production Results
Summary of Job ResultsInitial acid treatment created 50-60 of half-lengthSecond treatment created 200-220 of half-length (~200 short of design length) and produced close to prediction for about 1.5 years.Over time the half-length has decreased due to closure or recalcification to a length of 50-60 and is back on trend with production prior to second acid job.Conclusions:Second acid job was a huge success!Well could benefit from a third acid job!!