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SPE 106712
Case Study from 12 Successful Years of High Temperature
Fracturing in Bach Ho Field Offshore Vietnam
S. Jain, A. Prestridge, P. Dellorusso, N. C. Nghi
Schlumberger
D.D. Lam, V.Q. Hung
Viestsovpetro
SPE 106712
OUTLINEOUTLINE
• Introduction
• Reservoir Description
• Vessel Set-up
• Design, Execution, Evaluation
• Results & Discussion
• Conclusion
SPE 106712
IntroductionIntroduction
• Bach Ho field is located in the South China Sea, close to
Vung-Tau, Vietnam
• Field has 215 wells with an average seawater depth of 165 ft
• Production is from the Miocene, Oligocene and the Basement
formations
• Drilling practices and other damage mechanisms restrict
most wells from producing to their potential
SPE 106712
IntroductionIntroduction
• Propped fracturing is conducted in Oligocene whereas both
acidizing and fracturing have been tried in the Basement.
• High temperatures (>275oF), closure stress (>8,000 psi) and
operating from a vessel makes the execution of fracturing
treatments challenging.
SPE 106712
Reservoir DescriptionReservoir Description
• Average well depth - 12,500 ft
• Average porosity - 13 to 17%
• Permeability - 0.1 to 20 mD
• Water saturation - 10 to 15 %
• Presence of Migratory Clays
SPE 106712
Damage MechanismsDamage Mechanisms
• Completion Fluid
• Drilling Mud System
• Perforating Strategy
• Faulty Completion Practices
• Migratory Clays
Equipment SetEquipment Set--upup
Rental for vessels
ranges from $10,000
to $30,000/day
Equipment tailored
to enable faster rig-
up/rig-down
Vessel put together
for fracturing o/p in
8 days and the
demobilization was
completed in only 2
days
Storage
tanks
Lab. &
Monitoring unit
Proppant
Silo’s
POD
Coflexip
hose
Pumps
SPE 106712
Design ConsiderationsDesign Considerations
• Fracturing Fluid - Zirconate C/S-Linked
Polymeric Fluid
• Rheology - 110 cP at 170 sec-1 and 300°F
• Proppant - High Strength Proppant
• Fluid loss - 0.003 to 0.007 ft/min1/2
• Polymer Clean-up - Combination of encapsulated
and live breaker
SPE 106712
ExecutionExecution
• Diagnostic Tests
Wellbore Fill-up and Breakdown
Step-down
Step-Rate
Equilibrium
Calibration Test
• Main Fracture Treatment
SPE 106712
Treatment ParametersTreatment Parameters
• Treatment Rate - 20-25 bpm
• Proppant Concentration - 8-9 PPA
• Proppant Quantity - 60k to 80k lbs
• Diagnostic Tests - ~250 bbl (Linear)
~500 bbl (C/S)
• Treatment Volume - ~1500 bbls
• Pad Percentage - 40 to 75 %
SPE 106712
Case Study (Well A)Case Study (Well A)
• Target zone - Oligocene
• Total Vertical Depth (TVD) - 12,100 ft
• Perforation interval - 160 ft
• Shot density - 6 spf
• Permeability - 6 mD
• Porosity - 14%.
SPE 106712
Well A - Production History
0
200
400
600
800
1000
1200
1400
1600
Nov-04 Feb-05 May-05 Sep-05 Dec-05 Mar-06 Jul-06
Time
OilProduction(BOPD)
1400 bopd
(naturally
producing)
130 bopd
(gas-lift)
Production History
SPE 106712
0 15.0 30.0 45.0
0
2000.00
4000.00
6000.00
0
10.0
20.0
30.0
Treating Pressure (JobData)
Slurry Rate (JobData)
Proppant Conc (JobData)
Treating Pressure
Time (min)
Pressure(psi)
+
Step-Rate
Equilibrium
Test
Calibration
Injection
Calibration
Decline
Diagnostic TestsDiagnostic Tests
SPE 106712
0 6 12 18 24
6000
6400
6800
7200
7600
Rate - bbl/min
BottomHolePressure-psi
L1-S
L1-E
L2-S
L2-E
StepStep--Rate AnalysisRate Analysis
Frac. Extension
Pressure
Estimated
Closure Pr.
SPE 106712
0 0.5 1.0 1.5
6000
6200
6400
6600
6800
7000
0
500
1000
1500
2000
2500
Pre ssure De riva tive (dP/dG)
Supe rposition De riva tive (GdP/dG)
G Function
Pressure-psi
dP/dG&GdP/dG
Pc
ISIPL1-S
L1-E
L2-S
L2-E
Decline AnalysisDecline Analysis
Closure
Pressure
SPE 106712
Treatment Redesign
• Closure Pressure - 6600 psi
• Leak-off Coefficient - 0.006 ft/min1/2
• Fluid Efficiency - 12%
• Pad Percentage - 75%
SPE 106712
Fracturing TreatmentFracturing Treatment
Abnormal
Treating Pr.
7.0 47.0 87.0
0
2000.00
4000.00
6000.00
8000.00
10000.00
0
5.0
10.0
15.0
20.0
25.0
Treating Pressure Backup (JobData)
Slurry Rate (JobData)
Proppant Conc (JobData)
Treating Pressure
Time (min)
Pressure(psi)
Rate(bbl/min)
+
+
Proppant Stages
Abnormal
Treating Pr.
SPE 106712
Fracture Conductivity
SPE 106712
0.00
0.02
0.04
0.06
0.08
0.10
0.12
0.14
0.16
0.18
0 10 20 30 40 50 60 70 80 90 100
ProppedWidth-in
FractureHalf-Length- ft
0
2000
4000
6000
8000
10000
12000
Conductivity(Kfw)-md.ft
ProppedWidth(ACL) Conductivity- Kfw
Fracture Width vs. Half-Length
SPE 106712
Well A - Production History
0
200
400
600
800
1000
1200
1400
1600
Nov-04 Feb-05 May-05 Sep-05 Dec-05 Mar-06 Jul-06 Oct-06 Jan-07
Time
OilProduction(BOPD)
Post Frac.
Production
460 bopd
Pre Frac.
Production
130 bopd
Production History
SPE 106712
Abnormal Treating Pressures
• Higher Surface pressure
at the start of the main
treatment
• Undesirable due to high
HHP and surface treating
pressure limitations
• Poroelasticity and stress
concentration expected as
possible reasons 7.0 47.0
0
2000.00
4000.00
6000.00
8000.00
10000.00
TreatingPressureBa
SlurryRate(JobData)
ProppantConc(JobD
TreatingPressure
Time(min)
Pressure(psi)
+
3500psi
SPE 106712
Abnormal Treating Pressures
• Increase in closure pressure as a
result of increasing reservoir
pressure
• Large relatively clean zones,
combined with the fact that the
treating pressures decreased
within few minutes of the start of
the treatment does not support
poroelasticity as a possible factor
• Alteration in magnitude and
orientation of the in-situ stress
field locally, can be about
twice the effective stress.
• Crosslinked gel filter cake seals
the fracture face in the near
well-bore region, hence
pressure must exceed the
stress concentration effect
before a fracture can be
initiated
ppVH αασ
υ
υ
σ +−
−
= )(
1
Poroelasticity Stress Concentration
SPE 106712
0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
A1 A2 A3 A4 A5 A6 A7
Well Name
ProductivityIndex(bbl/day/psi)
Pre-Frac PI
Post Frac PI
Pre/Post Job PI Comparison
SPE 106712
0
100
200
300
400
500
600
A1 A2 A3 A4 A5 A6 A7
Well Name
lb/ftofproppantpumped
0
10
20
30
40
50
60
RatioofPI
lbs of prop. pumped / Net Height
Ratio of PI increase (normalized)
Quantity of Proppant/ft vs. PI Increase
SPE 106712
0
0.5
1
1.5
2
2.5
3
3.5
4
4.5
B1 B2 B3 B4 B5 B6 B7 B8 B9 B10
Well Name
PI(bbl/day/psi)
Pre Treatment PI
Post Treatment PI
Acid & Propped Frac.
Acid Fracturing
Acidizing
Comparison of PI for treatments in Basement
SPE 106712
ConclusionsConclusions
• Fracturing successfully implemented in the White Tiger
field with over 60 treatments performed at a success
rate greater than 85%.
• Average increase in Productivity Index of 5 times
• Propped fracturing has been successfully implemented in
Oligocene whereas high leak-off in the basement limits
its application in the latter.
SPE 106712
ConclusionsConclusions
• Abnormally high surface pressures observed in the start
of the treatment can be attributed to stress
concentration effects
• Higher volume of proppant pumped / feet of net height
results in higher PI thus indicating that bigger jobs can
improve NPV
• Acidizing results in improved productivity in the
basement but successfully executing propped fracturing
jobs with reasonable proppant volumes will result in
improved Productivity Index.
SPE 106712
Questions ?
SPE 106712
Case Study from 12 Successful Years of High Temperature
Fracturing in Bach Ho Field Offshore Vietnam
S. Jain, A. Prestridge, P. Dellorusso, N. C. Nghi
Schlumberger
D.D. Lam, V.Q. Hung
Viestsovpetro

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SPE 106712

  • 1. SPE 106712 Case Study from 12 Successful Years of High Temperature Fracturing in Bach Ho Field Offshore Vietnam S. Jain, A. Prestridge, P. Dellorusso, N. C. Nghi Schlumberger D.D. Lam, V.Q. Hung Viestsovpetro
  • 2. SPE 106712 OUTLINEOUTLINE • Introduction • Reservoir Description • Vessel Set-up • Design, Execution, Evaluation • Results & Discussion • Conclusion
  • 3. SPE 106712 IntroductionIntroduction • Bach Ho field is located in the South China Sea, close to Vung-Tau, Vietnam • Field has 215 wells with an average seawater depth of 165 ft • Production is from the Miocene, Oligocene and the Basement formations • Drilling practices and other damage mechanisms restrict most wells from producing to their potential
  • 4. SPE 106712 IntroductionIntroduction • Propped fracturing is conducted in Oligocene whereas both acidizing and fracturing have been tried in the Basement. • High temperatures (>275oF), closure stress (>8,000 psi) and operating from a vessel makes the execution of fracturing treatments challenging.
  • 5. SPE 106712 Reservoir DescriptionReservoir Description • Average well depth - 12,500 ft • Average porosity - 13 to 17% • Permeability - 0.1 to 20 mD • Water saturation - 10 to 15 % • Presence of Migratory Clays
  • 6. SPE 106712 Damage MechanismsDamage Mechanisms • Completion Fluid • Drilling Mud System • Perforating Strategy • Faulty Completion Practices • Migratory Clays
  • 7. Equipment SetEquipment Set--upup Rental for vessels ranges from $10,000 to $30,000/day Equipment tailored to enable faster rig- up/rig-down Vessel put together for fracturing o/p in 8 days and the demobilization was completed in only 2 days Storage tanks Lab. & Monitoring unit Proppant Silo’s POD Coflexip hose Pumps
  • 8. SPE 106712 Design ConsiderationsDesign Considerations • Fracturing Fluid - Zirconate C/S-Linked Polymeric Fluid • Rheology - 110 cP at 170 sec-1 and 300°F • Proppant - High Strength Proppant • Fluid loss - 0.003 to 0.007 ft/min1/2 • Polymer Clean-up - Combination of encapsulated and live breaker
  • 9. SPE 106712 ExecutionExecution • Diagnostic Tests Wellbore Fill-up and Breakdown Step-down Step-Rate Equilibrium Calibration Test • Main Fracture Treatment
  • 10. SPE 106712 Treatment ParametersTreatment Parameters • Treatment Rate - 20-25 bpm • Proppant Concentration - 8-9 PPA • Proppant Quantity - 60k to 80k lbs • Diagnostic Tests - ~250 bbl (Linear) ~500 bbl (C/S) • Treatment Volume - ~1500 bbls • Pad Percentage - 40 to 75 %
  • 11. SPE 106712 Case Study (Well A)Case Study (Well A) • Target zone - Oligocene • Total Vertical Depth (TVD) - 12,100 ft • Perforation interval - 160 ft • Shot density - 6 spf • Permeability - 6 mD • Porosity - 14%.
  • 12. SPE 106712 Well A - Production History 0 200 400 600 800 1000 1200 1400 1600 Nov-04 Feb-05 May-05 Sep-05 Dec-05 Mar-06 Jul-06 Time OilProduction(BOPD) 1400 bopd (naturally producing) 130 bopd (gas-lift) Production History
  • 13. SPE 106712 0 15.0 30.0 45.0 0 2000.00 4000.00 6000.00 0 10.0 20.0 30.0 Treating Pressure (JobData) Slurry Rate (JobData) Proppant Conc (JobData) Treating Pressure Time (min) Pressure(psi) + Step-Rate Equilibrium Test Calibration Injection Calibration Decline Diagnostic TestsDiagnostic Tests
  • 14. SPE 106712 0 6 12 18 24 6000 6400 6800 7200 7600 Rate - bbl/min BottomHolePressure-psi L1-S L1-E L2-S L2-E StepStep--Rate AnalysisRate Analysis Frac. Extension Pressure Estimated Closure Pr.
  • 15. SPE 106712 0 0.5 1.0 1.5 6000 6200 6400 6600 6800 7000 0 500 1000 1500 2000 2500 Pre ssure De riva tive (dP/dG) Supe rposition De riva tive (GdP/dG) G Function Pressure-psi dP/dG&GdP/dG Pc ISIPL1-S L1-E L2-S L2-E Decline AnalysisDecline Analysis Closure Pressure
  • 16. SPE 106712 Treatment Redesign • Closure Pressure - 6600 psi • Leak-off Coefficient - 0.006 ft/min1/2 • Fluid Efficiency - 12% • Pad Percentage - 75%
  • 17. SPE 106712 Fracturing TreatmentFracturing Treatment Abnormal Treating Pr. 7.0 47.0 87.0 0 2000.00 4000.00 6000.00 8000.00 10000.00 0 5.0 10.0 15.0 20.0 25.0 Treating Pressure Backup (JobData) Slurry Rate (JobData) Proppant Conc (JobData) Treating Pressure Time (min) Pressure(psi) Rate(bbl/min) + + Proppant Stages Abnormal Treating Pr.
  • 19. SPE 106712 0.00 0.02 0.04 0.06 0.08 0.10 0.12 0.14 0.16 0.18 0 10 20 30 40 50 60 70 80 90 100 ProppedWidth-in FractureHalf-Length- ft 0 2000 4000 6000 8000 10000 12000 Conductivity(Kfw)-md.ft ProppedWidth(ACL) Conductivity- Kfw Fracture Width vs. Half-Length
  • 20. SPE 106712 Well A - Production History 0 200 400 600 800 1000 1200 1400 1600 Nov-04 Feb-05 May-05 Sep-05 Dec-05 Mar-06 Jul-06 Oct-06 Jan-07 Time OilProduction(BOPD) Post Frac. Production 460 bopd Pre Frac. Production 130 bopd Production History
  • 21. SPE 106712 Abnormal Treating Pressures • Higher Surface pressure at the start of the main treatment • Undesirable due to high HHP and surface treating pressure limitations • Poroelasticity and stress concentration expected as possible reasons 7.0 47.0 0 2000.00 4000.00 6000.00 8000.00 10000.00 TreatingPressureBa SlurryRate(JobData) ProppantConc(JobD TreatingPressure Time(min) Pressure(psi) + 3500psi
  • 22. SPE 106712 Abnormal Treating Pressures • Increase in closure pressure as a result of increasing reservoir pressure • Large relatively clean zones, combined with the fact that the treating pressures decreased within few minutes of the start of the treatment does not support poroelasticity as a possible factor • Alteration in magnitude and orientation of the in-situ stress field locally, can be about twice the effective stress. • Crosslinked gel filter cake seals the fracture face in the near well-bore region, hence pressure must exceed the stress concentration effect before a fracture can be initiated ppVH αασ υ υ σ +− − = )( 1 Poroelasticity Stress Concentration
  • 23. SPE 106712 0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 A1 A2 A3 A4 A5 A6 A7 Well Name ProductivityIndex(bbl/day/psi) Pre-Frac PI Post Frac PI Pre/Post Job PI Comparison
  • 24. SPE 106712 0 100 200 300 400 500 600 A1 A2 A3 A4 A5 A6 A7 Well Name lb/ftofproppantpumped 0 10 20 30 40 50 60 RatioofPI lbs of prop. pumped / Net Height Ratio of PI increase (normalized) Quantity of Proppant/ft vs. PI Increase
  • 25. SPE 106712 0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 B1 B2 B3 B4 B5 B6 B7 B8 B9 B10 Well Name PI(bbl/day/psi) Pre Treatment PI Post Treatment PI Acid & Propped Frac. Acid Fracturing Acidizing Comparison of PI for treatments in Basement
  • 26. SPE 106712 ConclusionsConclusions • Fracturing successfully implemented in the White Tiger field with over 60 treatments performed at a success rate greater than 85%. • Average increase in Productivity Index of 5 times • Propped fracturing has been successfully implemented in Oligocene whereas high leak-off in the basement limits its application in the latter.
  • 27. SPE 106712 ConclusionsConclusions • Abnormally high surface pressures observed in the start of the treatment can be attributed to stress concentration effects • Higher volume of proppant pumped / feet of net height results in higher PI thus indicating that bigger jobs can improve NPV • Acidizing results in improved productivity in the basement but successfully executing propped fracturing jobs with reasonable proppant volumes will result in improved Productivity Index.
  • 29. SPE 106712 Case Study from 12 Successful Years of High Temperature Fracturing in Bach Ho Field Offshore Vietnam S. Jain, A. Prestridge, P. Dellorusso, N. C. Nghi Schlumberger D.D. Lam, V.Q. Hung Viestsovpetro