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Squeeze Cementing
Squeeze Definition
The placement of a cement
slurry under pressure against
a permeable formation
causing the slurry to
dehydrate and create a
cementitious seal across the
formation face.
Reasons For
Squeeze Cementing
Repair primary cement job
Channels
Voids due to losses
Shut-off produced water
Shut-off produced gas
Repair casing leaks
Abandon depleted zones
Selective shut-off for water
injection
Seal lost circulation zone
Shut off fluid migration
Squeeze Slurry
Design
Considerations:
Viscosity
Thickening time
Compressive strength
Fluid loss control
Squeeze pressure
Slurry volume
Primary Concerns
Squeeze Purpose
Formation Types
Establishing an Injection Rate
Method of Squeezing
Slurry Design
Laboratory Testing
Slurry Placement
Reasons for Failure
Good Habits
Pre-Job Meeting
Review Procedures
Discuss Potential Problems
Establish alternative Procedure
Good Record Keeping
Pressure
Times
Densities, Rates and Volumes
Cement Slurry
Viscosity
Low viscosity.
Entry into small fractures and
small cracks
Slurries using dispersants
preferred
High viscosity
Useful for cementing large voids
(vugs)
Will not flow into narrow
restrictions unless high pressure
applied
High gel strength restricts
movement of the slurry
Laboratory
Testing
Thickening Time
Always use Hesitation Squeeze
Schedule
Simulate Batch Mixing
Monitor Gelling Tendencies
Monitor Settling Tendencies
Modify API Schedule for Actual
Down Hole Conditions
Continue Hesitation until Slurry
Sets
Laboratory
Testing
Fluid Loss
Use Test Procedure in BJ Lab
Manual
Heat Slurry From Ambient
Above 200°F
 Condition in Pressurized
Consistometer or use Stirring
Fluid Loss Cell
Thickening Time
Required job time plus
reversal of excess cement
Temperature and pressure
Higher than in primary cementing
Use API squeeze schedules for
testing
Shallow wells
Short times (2 - 3 hours)
Use of accelerators
Deep wells and hesitation
squeezes
Long times (up to hours)
Compressive
Strength
High compressive strength
Withstand shocks from running
tools, drilling etc.
To prevent cracking during re-
perforation
Partially dehydrated cement
(filter cake)
Will develop sufficient strength
Not of primary concern
Fluid Loss
Control
Low pressure squeeze
Cement to fill all voids
Minimum node build up
Important with permeable
formations
Very low permeability
200 ml/30 minutes
Low / medium permeability
100 to 200 ml/30 minutes
High permeability (>100 md)
25 to 100 ml/30 minutes
Fluid Loss
Control (cont.)
High pressure squeeze
Medium to high permeability
200 to 500 ml/30 minutes
Fractured limestones, cement
travels large distance from
wellbore, re-perforation difficult:
High fluid loss rate
300 to 800 ml/30 minutes
Lost circulation material beneficial
Lead and tail (hesitate)
Lead 300 to 800 ml/ 30 min
Tail <300 ml/30 minutes
Cement
Node
Primary
Cement
Formation
Dehydrated
Cement
Casing
Cement
Nodes
FLUID LOSS
(∆P = 1,000 psi)
800 ml / 30 min
150 ml / 30 min
50 ml / 30 min
15 ml / 30 min
6 inch
Casing
Cement Node
Formation
Rate Of Filter
Cake Build Up
Permeability of the formation
Low = slow leak off
High = fast leak off
Differential pressure applied
Time over which pressure is
applied
Slurry fluid loss control
Low = slow dehydration
High = fast dehydration
Low permeability and fluid loss can
give excessive job times
High permeability and fluid loss
can cause bridges
Rate of Filter Cake
Build Up (cont.)
For a constant differential
pressure applied
Rate of cement filter cake growth
for a 30 md formation is
approximately twice that for a 300
md formation
For a given cement slurry, the
time taken to form a filter cake of
given thickness will double for a
ten fold decrease in formation
permeability
Filter Cake
Permeability
Lower fluid loss = lower cake
permeability = less solids filtered
out of slurry
Fluid Loss Time to Form Permeability
(API) 2.0 in. Cake
Neat cement < 30 sec. ± 5.0 md
300 cc < 4 min. ± 0.5 md
25 cc > 4 hours ± 0.05 md
Filter cake growth is indirectly
proportional to the cake's
permeability
Filter Cake
Permeability (cont.)
Squeeze pressure
Increasing squeeze pressure
does not reduce the permeability
of the filter cake
Flow of filtrate through a filter
cake is proportional to the
permeability of that cake
Darcy's law
Flow rate through filter cake of
given permeability is proportional
to the differential pressure
Cement Slurry
Volume
Dependent upon length of
interval to be squeezed
For job convenience 10 to 20
barrels are prepared
Volume for high pressure
squeezes should be
minimized
Fracture at low pump rate
Keep pressure below fracture
propagation pressure
Cement Slurry
Volume (cont.)
Rules of thumb:
Cement volume should not
exceed capacity of treating string
Use two sacks of cement per foot
of perforations
If injection rate after break down
is 2.0 bpm or more:
Minimum volume 100 sacks
If injection rate after break down
is less than 2.0 bpm:
Minimum volume 50 sacks
Planning
Establish Two-Rate Fluid
Injection Profile
Determine Fracture Gradient
Determine BHSqT
Determine Top of Existing
Cement
Determine Formation Pore
Pressure
Planning - Cont.
Determine Formation Fluid
Characteristics
Calculate Hydrostatic
Pressure Differential
Review Completion Records
“Gather Data Before Designing a
Cement Slurry”
Injectivity
Viscosity must be manageable
Channel repair may require
small cement particle sizes
Injection Testing
Use water, chemical flush or
weak acid
Used to ensure all
perforations are open
Helps to estimate slurry
injection rate
Helps to estimate pressure for
performing squeeze
Helps to estimate cement
volume required
If injection is not achieved, an
acid perforation wash should
be performed under matrix
conditions
Establishing An
Injection
Pump at a Constant Slow Rate
Increase rate to Obtain
Desired Cement Placement
Rate
“Remember not to Exceed Fracture
Gradient !”
Why Establish
Injection Rate
To determine if and at what
rate “BELOW THE FRACTURE
GRADIENT” fluid can be
placed against the formation.
Two Rate
Injection
Lowest Rate at which the
Formation will take Fluid
Minimum Rate needed to
Displace Cement to the First
Hesitation
Always Establish with Clear Fluid
Avoid using Mud
Variable
Affects Rate
Choice
Thickening Time
Packer Depth
Slurry Volume
Depth
Workstring Size
Casing Size
When Fracture
Pressure Is
Unavoidable !
REMEMBER
You Will Damage the Formation
You Will Increase the Difficulty of
getting a Satisfactory Job
The Key is to
“BE CONSERVATIVE”
Proper Execution
High Injection Rate - Low
Pump Pressure
High Pump Pressure - Low
Injection Rates
Types Of
Injection Rates
Loose Injection Rates
High Rates
Low Pressures
Tight Injection Rates
Low Rates
High Pressures
6 to 8 BPM
0 - 200 PSI
0.25 - 0.5 BPM
3500 - 4000 PSI
Loose Injection Tight Injection
Injection Rates And Pressures
Injection Rate
Profile
From Chevron DTC
Caution
“ High injection rates with
high pressures”
Almost Never Acceptable!
Yields highly fractured formations
that require a large volume of
cement slurry, before actually
obtaining a squeeze.
Reasons For
Failure
Non-Determination of
Injection Rate
Slurry Design and Testing
Slurry Placement Problems
Squeeze Cementing
Methods
Principal methods:
Squeeze packers
Cement retainers
Bradenhead
Modes of operation:
Low pressure
High pressure
Job procedures:
Running squeeze
Hesitation squeeze
Packer or Retainer
Setting Depth
Determine from CBL
Using tail pipe:
Minimum distance from top perforation is
limited by tail pipe length
Do not set tool too close to top
perforation:
Communication in annulus above tool
can collapse casing
Do not set packer too high (running
squeeze):
Minimize contamination with mud or
other fluids
Minimum 30 ft 75 feet above top
perforation
Retrievable
Packers
Compression or tension set
packers are used for squeeze
cementing
Packer should have by-pass valve
to:
Allow fluid circulation when running in
hole
Clean tool after job
Allow reversing of excess cement slurry
Prevent swabbing
Flexible, can set and release many
times
Can run in tandem with retrievable
bridge plugs
Place sand on top of bridge plug
Viscous Pill
Mud
Mud
Packer
Spacer
Viscous Pill
Cement
Squeeze Through A
Packer Balanced Plug
Method
Spot viscous pill
Pull to top of pill
Spot cement and spacer as balanced plug
Under displace (1 to 2 barrels) to ensure
flow out of the drill pipe
Mud
Mud
Viscous Pill
Cement
Mud
Packer
Spacer
Squeeze Through A
Packer Balanced Plug
Method
Pull out above top of cement (500 ft)
Set the packer and squeeze cement
When squeeze complete, unset the packer
Reverse circulate any excess cement and
spacer out of hole
Drillable
Cement Retainer
Prevent back flow where no cement
dehydration is expected (circulating
squeeze into channels)
Used where high differential pressure may
disturb the filter cake
Where communication with upper
perforated zone makes use of packers
risky
Multiple zones, isolates lower zone
Allow further squeeze operations without
waiting on cement.
Can be set closer to the perforations (Less
fluid injected ahead)
Mud
Mud
Retainer
Running Squeeze
Method Through A
Cement Retainer
Run in hole with retainer on wireline or
drill pipe
Set retainer
If wireline set, run in hole with drill pipe
If run on drill pipe sting out from retainer
Viscous Pill
Mud
Mud
Cement
Retainer
Spacer
Running Squeeze Method
Through A Cement
Retainer (cont.)
Circulate cement down to
bottom of drill pipe
Sting into the retainer and
squeeze cement
Cement
Viscous Pill
Mud
Mud
Cement
Retainer
Running Squeeze Method
Through A Cement
Retainer (cont.)
Sting out from retainer and
reverse circulate excess
cement and spacer
Pull out of hole
Bullhead Squeeze
Method
Casing
Pump
500 - 1000
psi
Casing Pump
500 - 1000 psi
Cement
Displacement
Fluid
Mud or
Displacement
Fluid
 Pump cement
with packer Set
 Displace Mud
into Formation
 Hold Annulus
Pressure
 Apply Squeeze
Pressure
Spotting Method
Casing Pump
500 - 1000 psi
 Sting out of tool
 Spot cement
 Stab with Packer
 Apply Casing
Pressure
 Displace
Cement
 Apply Squeeze
Pressure
Bradenhead Squeeze
Technique
Used when low pressure
squeezing is practiced
Used where casing and
surface equipment have
sufficient burst resistance to
withstand squeeze pressures
This is the most popular
method due to its simplicity
Bradenhead
Method
 Spot Cement
 Pull Work
String
 Close Annulus
 Apply Squeeze
Pressure
Coiled Tubing
Operations
(Through Tubing Squeezes)
Advantages
Time Savings
Cost Savings
Pumping Flexibility
Fluid Placement
Reduced Formation Damage
Safety
Coiled Tubing
Applications
Well Stimulation
Wireline and Production
Logging
Perforating
Squeeze Cementing
Fill Cleanup
Sand Consolidation
Cement Requirements
for Coiled Tubing
Squeeze
Fluid Loss
< 60 and > 30 cc’s/30 min.
Compressive Strength
1000 psi in 12 Hrs.
Thickening Time
6 - 8 Hours at BHTT
Free Water
Zero cc’s at 45° Angle
Cement Requirements
for Coiled Tubing
Squeeze (cont.)
Rheologies
@ R.T.
PV; 200 to 350
YP; 70 to 130
@ BHTT
PV; 70 to 130
YP; 10 to 25
Nodes
0.75 to 1 inch
Firm Cake
Mud Placement
 Placement of Mud
 Pull Nozzle Up while
Pumping, to Maintain
Mud-Brine Interface
10 - 15’ Above Nozzle
 Pump 1 BBL. Excess
 Locate Top of Mud
 Fluid Pac the Well
 Wash Out
Contaminated Mud
 Identify Top of Mud
Viscous Pill
Perforations
Brine Fluid
Cement Placement
and Squeeze
 Circulate in Cement
 Pull Nozzle Up while Pumping
Cement, to Maintain Cmt/Mud
Interface 100’ Above Nozzle
 Cement Volume from
Evaluation Log
 Pull Nozzle Above Cement
 Close Annulus and Squeeze
 Squeeze Pressure at 1500 to
2000 psi above Reservoir
Pressure and Hold for
40 Minutes
Viscous Pill
Cement
Perforations
Fresh Water
Brine Fluid
Contaminating
The Cement
 Pump contaminant
and Lower the Nozzle to
Displace 1 BBL of
Cement per BBL of
Contaminant
Contaminate 50’ into Mud
Pull Nozzle up and Pump
Contaminant at a Rate of
1 BBL per 2 - 3 BBL of
Previously Contaminated
Cement
Contaminant
Cement / Contaminant
(50/50)
Dehydrated Cement
Nodes
Mud / Contaminant
(50/50)
Dehydrated
Cement nodes
Mud, Cement
and
Contaminant
Viscous Pill
Reversing Out
Contaminated Cement
to be Reversed out the
Following Day or After
Cement has Set
Jet with Fresh Water
While Going Down 50’
Below the Original Mud
Top
Reverse out and Pull
Nozzle at a Rate to
Circulate out 1 BBL per
BBL pumped
Repeat Reverse out 2
more Times or Until
Returns Cleanup
Evaluate with CET,
Repeat if Necessary
If OK, Reperforate and
Test
Low Pressure
Squeeze Cementing
Bottom hole treating pressure maintained
below fracture pressure
Aim to fill perforations and connected
cavities with dehydrated cement
Cement volume is small
Hydrostatic control is required to prevent
formation breakdown
Use safety factor of 500 psi
Low pump rates
Friction pressure is negligible
Perforations must be clean and free of
mud or solids
Cement nodes should be small
High Pressure
Squeeze Cementing
Bottom hole treating pressure is higher
than fracture pressure
Fractures created at or close to
perforations
Fluid ahead of cement is displaced into
fracture
Cement slurry fills the fracture and any
voids or connecting channels
Further applied pressure dehydrates the
cement against fracture walls
When final squeeze pressure is applied all
channels should be filled with cement
filter cake
Extreme Losses
Sodium Silicate Pre-Flush
(Flow-Guard)
Pump CaCl Pad
Pump Fresh Water Pad
Pump Flow-Guard
Pump Fresh Water Pad
Pump Cement Design
One Possible Situation for
“Neat” Cement
Low fluid loss = good frac!
Use Caution with Sodium
Silicate Across Pay Interval
Running Squeeze
Misconceptions
Formation Locks-up at High Rates
Final Squeeze Pressure Must be
Obtained at the Rate Induced During
Injection
Better Term “Walking” or
“Creeping”
More Applicable for Low
Permeability Formations
Always Know the Location of the
Cement
Know the  P between Cement &
Wellbore face
When To High
Pressure Squeeze
Where voids and channels
cement behind casing are not
connected to the perforations
Where small cracks or micro-
annuli allow passage of gas
but will not take cement
Application of Ultra Fine cements
Perforations are plugged or
debris ahead of cement
cannot be removed
High Pressure
Squeezes (cont.)
Extent of the induced fracture is a
function of pump rate
Slurry volume is dependent upon pump
rate:
High rate = large fracture
Large fractures = large volumes
Minimum volumes should be used to
allow perforation past cement where
required
Drilling mud or low fluid loss fluids
should not be pumped ahead
Use weak acid or water as a pre-flush
Related Fracture
Theory
Location and orientation of created
fracture cannot be controlled
Fractures occur in plane
perpendicular to direction of least
resistance
In most wells overburden is the
principle stress, vertical fractures
result.
Fracturing pressure is less than
overburden
In shallow wells (< 3000 ft)
horizontal fractures can occur
Fracturing pressure is greater than
overburden
σ H2
σ H1
PF
σ Over-burden
High Pressure
Squeeze Fracture
Orientation
Where fracture pressure is less
than over-burden pressure
Primary
Cement
Cement
Filter Cake
Mud
Filtrate
Filtrate
Mud
Vertical
Fracture
Dehydrated
Cement
Casing
Running Squeeze
Cement slurry pumped continuously until
final squeeze pressure is achieved
This may be above fracture pressure
When pumping is stopped, final squeeze
pressure is maintained and monitored
Pressure drop due to filtrate leak off
should be re-applied up to final squeeze
pressure
Repeat procedure as necessary until
pressure remains steady for several
minutes
Volumes are large 10 to 100 barrels
Hesitation
Squeeze
Only practical method for small volumes
Intermittent application of pressure at low
rates
0.25 to 0.5 bpm
Each application of pressure is separated
by a period of shut-down to allow for
filtrate leak-off
10 to 20 minutes
Initial leak-off is high
As cake builds up and applied pressure
increases, leak-off slows down
As several hesitations are applied, the
difference between initial pressure and
final pressure becomes smaller
2,400
2,000
1,600
1,200
800
400
0
0 20 40 60 80 100 120 140 160
SurfacePressure,psi
Time, minutes
A
B C D
Hesitation Squeeze
Pressure Behavior
A = Slurry mix-water leaks off
B = No slurry mix-water filtrates
therefore squeeze is complete
C = Pressure is bled off
D = Final pressure test
Hesitation Squeeze Profile
Loose Injection Rate
1 2 3 4
1000
2000
0
PRESSURE
TIME in HOURS
Pump as slow as possible
( 1/4 to 1/2 BPM )
Chevron DTC
Hesitation Squeeze Profile
Tight Injection Rate
2000
1000
0 1 2
TIME in HOURS
PRESSURE
( 1/4 to 1/2 BPM )
Chevron DTC
Best Results
“Always Plan for a Hesitation
Squeeze, But be prepared for
a Running Squeeze”
CFL
Two Slurry Method
Conventional Method
Lead Slurry: Fluid Loss < 100 cc’s
Tail Slurry: No Fluid Loss Control
Modified Method
(Chevron DTC)
Lead Slurry: Mod. Fluid Loss -
300 to 500 cc’s
Tail Slurry: Fluid Loss < 100 cc’s
More Specifics to follow...
CFL Slurry Design
Modified Method
(Chevron DTC)
Loose Injection
Lead Slurry
Fluid Loss 300 to 500 cc’s
Thickening Time
 1 to 2.5 hours
Free Water & Comp. Strength - N/A
Tail Slurry
Fluid Loss < 100 cc’s
Thickening Time
 3 - 5 hours (Hesitation
Schedule)
Free Water & Comp. Strength - N/A
Modified Method
Loose Injection Tight Injection
CFL Two Slurry Method LWL Single Slurry Method
Lead : 500. . . . . . 300 . . . . . 200. . . . . . . N.A.
Tail : < 100. . . . . . .100 . . . . 100 . . . . . . . 100
Fluid Loss Control
Chevron DTC
Calculating Pressure
to Reverse-Out
Always know what pressures are
required to reverse-out.
Step 1: Calculate Differential Fluid
Gradient, psi/ft
15.6 ppg x 0.052 = 0.8112 psi/ft ( Cement )
10.0 ppg x 0.052 = 0.5200 psi/ft ( Comp Fluid )
0.2912 psi/ft
Step II: Determine Tubing Fill
Factor, ft/bbl (decimal book)
2-3/8” 4.7 lbs/ft tubing = 258.65 ft/bbl of fill
Step III: Calculate Pressure to
Reverse-Out, psi/bbl
ex: 258.65 ft/bbl x 0.2912 psi/ft = 75.3 psi/bbl*
*Multiple psi/bbl by the barrels
of slurry left in the tubing
Hesitation
Squeeze
Final squeeze is achieved
when the leak-off becomes
negligible
For loose, permeable
formations a first hesitation
period of up to 30 minutes is
not unreasonable
For tight low permeability
formations a short first
hesitation period of ± 5
minutes is sufficient
Hesitation
Squeeze
(Chevron DTC)
Always Test on Hesitation
Schedule
Hesitation Time Dictated by
Pressure Build-up
Be Patient
Use CFL Slurry
Know the Location of the
Cement
Never Over-Displace
Determine Final Squeeze
Pressure from Injection Profile
Misconceptions of
Squeeze Cementing
Cement slurry enters
formation pore spaces
All perforations are open
High pressure squeezes
create horizontal pancake
High final pressure is required
to assure success
Final squeeze pressure must
equal future working pressure
General
Recommendations
Ensure hole is junk free
Ensure perforations are open
Acid wash if necessary
Low pressure squeeze where
possible
Use low fluid loss cement
Cement volume should not exceed
string volume
High final squeeze pressure is not
essential
Batch mix cement
Allow adequate time for cement to
set based on compressive strength
data

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Squeeze cementing

  • 2. Squeeze Definition The placement of a cement slurry under pressure against a permeable formation causing the slurry to dehydrate and create a cementitious seal across the formation face.
  • 3. Reasons For Squeeze Cementing Repair primary cement job Channels Voids due to losses Shut-off produced water Shut-off produced gas Repair casing leaks Abandon depleted zones Selective shut-off for water injection Seal lost circulation zone Shut off fluid migration
  • 4. Squeeze Slurry Design Considerations: Viscosity Thickening time Compressive strength Fluid loss control Squeeze pressure Slurry volume
  • 5. Primary Concerns Squeeze Purpose Formation Types Establishing an Injection Rate Method of Squeezing Slurry Design Laboratory Testing Slurry Placement Reasons for Failure
  • 6. Good Habits Pre-Job Meeting Review Procedures Discuss Potential Problems Establish alternative Procedure Good Record Keeping Pressure Times Densities, Rates and Volumes
  • 7. Cement Slurry Viscosity Low viscosity. Entry into small fractures and small cracks Slurries using dispersants preferred High viscosity Useful for cementing large voids (vugs) Will not flow into narrow restrictions unless high pressure applied High gel strength restricts movement of the slurry
  • 8. Laboratory Testing Thickening Time Always use Hesitation Squeeze Schedule Simulate Batch Mixing Monitor Gelling Tendencies Monitor Settling Tendencies Modify API Schedule for Actual Down Hole Conditions Continue Hesitation until Slurry Sets
  • 9. Laboratory Testing Fluid Loss Use Test Procedure in BJ Lab Manual Heat Slurry From Ambient Above 200°F  Condition in Pressurized Consistometer or use Stirring Fluid Loss Cell
  • 10. Thickening Time Required job time plus reversal of excess cement Temperature and pressure Higher than in primary cementing Use API squeeze schedules for testing Shallow wells Short times (2 - 3 hours) Use of accelerators Deep wells and hesitation squeezes Long times (up to hours)
  • 11. Compressive Strength High compressive strength Withstand shocks from running tools, drilling etc. To prevent cracking during re- perforation Partially dehydrated cement (filter cake) Will develop sufficient strength Not of primary concern
  • 12. Fluid Loss Control Low pressure squeeze Cement to fill all voids Minimum node build up Important with permeable formations Very low permeability 200 ml/30 minutes Low / medium permeability 100 to 200 ml/30 minutes High permeability (>100 md) 25 to 100 ml/30 minutes
  • 13. Fluid Loss Control (cont.) High pressure squeeze Medium to high permeability 200 to 500 ml/30 minutes Fractured limestones, cement travels large distance from wellbore, re-perforation difficult: High fluid loss rate 300 to 800 ml/30 minutes Lost circulation material beneficial Lead and tail (hesitate) Lead 300 to 800 ml/ 30 min Tail <300 ml/30 minutes
  • 14. Cement Node Primary Cement Formation Dehydrated Cement Casing Cement Nodes FLUID LOSS (∆P = 1,000 psi) 800 ml / 30 min 150 ml / 30 min 50 ml / 30 min 15 ml / 30 min 6 inch Casing Cement Node Formation
  • 15. Rate Of Filter Cake Build Up Permeability of the formation Low = slow leak off High = fast leak off Differential pressure applied Time over which pressure is applied Slurry fluid loss control Low = slow dehydration High = fast dehydration Low permeability and fluid loss can give excessive job times High permeability and fluid loss can cause bridges
  • 16. Rate of Filter Cake Build Up (cont.) For a constant differential pressure applied Rate of cement filter cake growth for a 30 md formation is approximately twice that for a 300 md formation For a given cement slurry, the time taken to form a filter cake of given thickness will double for a ten fold decrease in formation permeability
  • 17. Filter Cake Permeability Lower fluid loss = lower cake permeability = less solids filtered out of slurry Fluid Loss Time to Form Permeability (API) 2.0 in. Cake Neat cement < 30 sec. ± 5.0 md 300 cc < 4 min. ± 0.5 md 25 cc > 4 hours ± 0.05 md Filter cake growth is indirectly proportional to the cake's permeability
  • 18. Filter Cake Permeability (cont.) Squeeze pressure Increasing squeeze pressure does not reduce the permeability of the filter cake Flow of filtrate through a filter cake is proportional to the permeability of that cake Darcy's law Flow rate through filter cake of given permeability is proportional to the differential pressure
  • 19. Cement Slurry Volume Dependent upon length of interval to be squeezed For job convenience 10 to 20 barrels are prepared Volume for high pressure squeezes should be minimized Fracture at low pump rate Keep pressure below fracture propagation pressure
  • 20. Cement Slurry Volume (cont.) Rules of thumb: Cement volume should not exceed capacity of treating string Use two sacks of cement per foot of perforations If injection rate after break down is 2.0 bpm or more: Minimum volume 100 sacks If injection rate after break down is less than 2.0 bpm: Minimum volume 50 sacks
  • 21. Planning Establish Two-Rate Fluid Injection Profile Determine Fracture Gradient Determine BHSqT Determine Top of Existing Cement Determine Formation Pore Pressure
  • 22. Planning - Cont. Determine Formation Fluid Characteristics Calculate Hydrostatic Pressure Differential Review Completion Records “Gather Data Before Designing a Cement Slurry”
  • 23. Injectivity Viscosity must be manageable Channel repair may require small cement particle sizes
  • 24. Injection Testing Use water, chemical flush or weak acid Used to ensure all perforations are open Helps to estimate slurry injection rate Helps to estimate pressure for performing squeeze Helps to estimate cement volume required If injection is not achieved, an acid perforation wash should be performed under matrix conditions
  • 25. Establishing An Injection Pump at a Constant Slow Rate Increase rate to Obtain Desired Cement Placement Rate “Remember not to Exceed Fracture Gradient !”
  • 26. Why Establish Injection Rate To determine if and at what rate “BELOW THE FRACTURE GRADIENT” fluid can be placed against the formation.
  • 27. Two Rate Injection Lowest Rate at which the Formation will take Fluid Minimum Rate needed to Displace Cement to the First Hesitation Always Establish with Clear Fluid Avoid using Mud
  • 28. Variable Affects Rate Choice Thickening Time Packer Depth Slurry Volume Depth Workstring Size Casing Size
  • 29. When Fracture Pressure Is Unavoidable ! REMEMBER You Will Damage the Formation You Will Increase the Difficulty of getting a Satisfactory Job The Key is to “BE CONSERVATIVE”
  • 30. Proper Execution High Injection Rate - Low Pump Pressure High Pump Pressure - Low Injection Rates
  • 31. Types Of Injection Rates Loose Injection Rates High Rates Low Pressures Tight Injection Rates Low Rates High Pressures
  • 32. 6 to 8 BPM 0 - 200 PSI 0.25 - 0.5 BPM 3500 - 4000 PSI Loose Injection Tight Injection Injection Rates And Pressures Injection Rate Profile From Chevron DTC
  • 33. Caution “ High injection rates with high pressures” Almost Never Acceptable! Yields highly fractured formations that require a large volume of cement slurry, before actually obtaining a squeeze.
  • 34. Reasons For Failure Non-Determination of Injection Rate Slurry Design and Testing Slurry Placement Problems
  • 35. Squeeze Cementing Methods Principal methods: Squeeze packers Cement retainers Bradenhead Modes of operation: Low pressure High pressure Job procedures: Running squeeze Hesitation squeeze
  • 36. Packer or Retainer Setting Depth Determine from CBL Using tail pipe: Minimum distance from top perforation is limited by tail pipe length Do not set tool too close to top perforation: Communication in annulus above tool can collapse casing Do not set packer too high (running squeeze): Minimize contamination with mud or other fluids Minimum 30 ft 75 feet above top perforation
  • 37. Retrievable Packers Compression or tension set packers are used for squeeze cementing Packer should have by-pass valve to: Allow fluid circulation when running in hole Clean tool after job Allow reversing of excess cement slurry Prevent swabbing Flexible, can set and release many times Can run in tandem with retrievable bridge plugs Place sand on top of bridge plug
  • 38. Viscous Pill Mud Mud Packer Spacer Viscous Pill Cement Squeeze Through A Packer Balanced Plug Method Spot viscous pill Pull to top of pill Spot cement and spacer as balanced plug Under displace (1 to 2 barrels) to ensure flow out of the drill pipe
  • 39. Mud Mud Viscous Pill Cement Mud Packer Spacer Squeeze Through A Packer Balanced Plug Method Pull out above top of cement (500 ft) Set the packer and squeeze cement When squeeze complete, unset the packer Reverse circulate any excess cement and spacer out of hole
  • 40. Drillable Cement Retainer Prevent back flow where no cement dehydration is expected (circulating squeeze into channels) Used where high differential pressure may disturb the filter cake Where communication with upper perforated zone makes use of packers risky Multiple zones, isolates lower zone Allow further squeeze operations without waiting on cement. Can be set closer to the perforations (Less fluid injected ahead)
  • 41. Mud Mud Retainer Running Squeeze Method Through A Cement Retainer Run in hole with retainer on wireline or drill pipe Set retainer If wireline set, run in hole with drill pipe If run on drill pipe sting out from retainer
  • 42. Viscous Pill Mud Mud Cement Retainer Spacer Running Squeeze Method Through A Cement Retainer (cont.) Circulate cement down to bottom of drill pipe Sting into the retainer and squeeze cement Cement
  • 43. Viscous Pill Mud Mud Cement Retainer Running Squeeze Method Through A Cement Retainer (cont.) Sting out from retainer and reverse circulate excess cement and spacer Pull out of hole
  • 44. Bullhead Squeeze Method Casing Pump 500 - 1000 psi Casing Pump 500 - 1000 psi Cement Displacement Fluid Mud or Displacement Fluid  Pump cement with packer Set  Displace Mud into Formation  Hold Annulus Pressure  Apply Squeeze Pressure
  • 45. Spotting Method Casing Pump 500 - 1000 psi  Sting out of tool  Spot cement  Stab with Packer  Apply Casing Pressure  Displace Cement  Apply Squeeze Pressure
  • 46. Bradenhead Squeeze Technique Used when low pressure squeezing is practiced Used where casing and surface equipment have sufficient burst resistance to withstand squeeze pressures This is the most popular method due to its simplicity
  • 47. Bradenhead Method  Spot Cement  Pull Work String  Close Annulus  Apply Squeeze Pressure
  • 48. Coiled Tubing Operations (Through Tubing Squeezes) Advantages Time Savings Cost Savings Pumping Flexibility Fluid Placement Reduced Formation Damage Safety
  • 49. Coiled Tubing Applications Well Stimulation Wireline and Production Logging Perforating Squeeze Cementing Fill Cleanup Sand Consolidation
  • 50. Cement Requirements for Coiled Tubing Squeeze Fluid Loss < 60 and > 30 cc’s/30 min. Compressive Strength 1000 psi in 12 Hrs. Thickening Time 6 - 8 Hours at BHTT Free Water Zero cc’s at 45° Angle
  • 51. Cement Requirements for Coiled Tubing Squeeze (cont.) Rheologies @ R.T. PV; 200 to 350 YP; 70 to 130 @ BHTT PV; 70 to 130 YP; 10 to 25 Nodes 0.75 to 1 inch Firm Cake
  • 52. Mud Placement  Placement of Mud  Pull Nozzle Up while Pumping, to Maintain Mud-Brine Interface 10 - 15’ Above Nozzle  Pump 1 BBL. Excess  Locate Top of Mud  Fluid Pac the Well  Wash Out Contaminated Mud  Identify Top of Mud Viscous Pill Perforations Brine Fluid
  • 53. Cement Placement and Squeeze  Circulate in Cement  Pull Nozzle Up while Pumping Cement, to Maintain Cmt/Mud Interface 100’ Above Nozzle  Cement Volume from Evaluation Log  Pull Nozzle Above Cement  Close Annulus and Squeeze  Squeeze Pressure at 1500 to 2000 psi above Reservoir Pressure and Hold for 40 Minutes Viscous Pill Cement Perforations Fresh Water Brine Fluid
  • 54. Contaminating The Cement  Pump contaminant and Lower the Nozzle to Displace 1 BBL of Cement per BBL of Contaminant Contaminate 50’ into Mud Pull Nozzle up and Pump Contaminant at a Rate of 1 BBL per 2 - 3 BBL of Previously Contaminated Cement Contaminant Cement / Contaminant (50/50) Dehydrated Cement Nodes Mud / Contaminant (50/50)
  • 55. Dehydrated Cement nodes Mud, Cement and Contaminant Viscous Pill Reversing Out Contaminated Cement to be Reversed out the Following Day or After Cement has Set Jet with Fresh Water While Going Down 50’ Below the Original Mud Top Reverse out and Pull Nozzle at a Rate to Circulate out 1 BBL per BBL pumped Repeat Reverse out 2 more Times or Until Returns Cleanup Evaluate with CET, Repeat if Necessary If OK, Reperforate and Test
  • 56. Low Pressure Squeeze Cementing Bottom hole treating pressure maintained below fracture pressure Aim to fill perforations and connected cavities with dehydrated cement Cement volume is small Hydrostatic control is required to prevent formation breakdown Use safety factor of 500 psi Low pump rates Friction pressure is negligible Perforations must be clean and free of mud or solids Cement nodes should be small
  • 57. High Pressure Squeeze Cementing Bottom hole treating pressure is higher than fracture pressure Fractures created at or close to perforations Fluid ahead of cement is displaced into fracture Cement slurry fills the fracture and any voids or connecting channels Further applied pressure dehydrates the cement against fracture walls When final squeeze pressure is applied all channels should be filled with cement filter cake
  • 58. Extreme Losses Sodium Silicate Pre-Flush (Flow-Guard) Pump CaCl Pad Pump Fresh Water Pad Pump Flow-Guard Pump Fresh Water Pad Pump Cement Design One Possible Situation for “Neat” Cement Low fluid loss = good frac! Use Caution with Sodium Silicate Across Pay Interval
  • 59. Running Squeeze Misconceptions Formation Locks-up at High Rates Final Squeeze Pressure Must be Obtained at the Rate Induced During Injection Better Term “Walking” or “Creeping” More Applicable for Low Permeability Formations Always Know the Location of the Cement Know the  P between Cement & Wellbore face
  • 60. When To High Pressure Squeeze Where voids and channels cement behind casing are not connected to the perforations Where small cracks or micro- annuli allow passage of gas but will not take cement Application of Ultra Fine cements Perforations are plugged or debris ahead of cement cannot be removed
  • 61. High Pressure Squeezes (cont.) Extent of the induced fracture is a function of pump rate Slurry volume is dependent upon pump rate: High rate = large fracture Large fractures = large volumes Minimum volumes should be used to allow perforation past cement where required Drilling mud or low fluid loss fluids should not be pumped ahead Use weak acid or water as a pre-flush
  • 62. Related Fracture Theory Location and orientation of created fracture cannot be controlled Fractures occur in plane perpendicular to direction of least resistance In most wells overburden is the principle stress, vertical fractures result. Fracturing pressure is less than overburden In shallow wells (< 3000 ft) horizontal fractures can occur Fracturing pressure is greater than overburden
  • 63. σ H2 σ H1 PF σ Over-burden High Pressure Squeeze Fracture Orientation Where fracture pressure is less than over-burden pressure Primary Cement Cement Filter Cake Mud Filtrate Filtrate Mud Vertical Fracture Dehydrated Cement Casing
  • 64. Running Squeeze Cement slurry pumped continuously until final squeeze pressure is achieved This may be above fracture pressure When pumping is stopped, final squeeze pressure is maintained and monitored Pressure drop due to filtrate leak off should be re-applied up to final squeeze pressure Repeat procedure as necessary until pressure remains steady for several minutes Volumes are large 10 to 100 barrels
  • 65. Hesitation Squeeze Only practical method for small volumes Intermittent application of pressure at low rates 0.25 to 0.5 bpm Each application of pressure is separated by a period of shut-down to allow for filtrate leak-off 10 to 20 minutes Initial leak-off is high As cake builds up and applied pressure increases, leak-off slows down As several hesitations are applied, the difference between initial pressure and final pressure becomes smaller
  • 66. 2,400 2,000 1,600 1,200 800 400 0 0 20 40 60 80 100 120 140 160 SurfacePressure,psi Time, minutes A B C D Hesitation Squeeze Pressure Behavior A = Slurry mix-water leaks off B = No slurry mix-water filtrates therefore squeeze is complete C = Pressure is bled off D = Final pressure test
  • 67. Hesitation Squeeze Profile Loose Injection Rate 1 2 3 4 1000 2000 0 PRESSURE TIME in HOURS Pump as slow as possible ( 1/4 to 1/2 BPM ) Chevron DTC
  • 68. Hesitation Squeeze Profile Tight Injection Rate 2000 1000 0 1 2 TIME in HOURS PRESSURE ( 1/4 to 1/2 BPM ) Chevron DTC
  • 69. Best Results “Always Plan for a Hesitation Squeeze, But be prepared for a Running Squeeze”
  • 70. CFL Two Slurry Method Conventional Method Lead Slurry: Fluid Loss < 100 cc’s Tail Slurry: No Fluid Loss Control Modified Method (Chevron DTC) Lead Slurry: Mod. Fluid Loss - 300 to 500 cc’s Tail Slurry: Fluid Loss < 100 cc’s More Specifics to follow...
  • 71. CFL Slurry Design Modified Method (Chevron DTC) Loose Injection Lead Slurry Fluid Loss 300 to 500 cc’s Thickening Time  1 to 2.5 hours Free Water & Comp. Strength - N/A Tail Slurry Fluid Loss < 100 cc’s Thickening Time  3 - 5 hours (Hesitation Schedule) Free Water & Comp. Strength - N/A
  • 72. Modified Method Loose Injection Tight Injection CFL Two Slurry Method LWL Single Slurry Method Lead : 500. . . . . . 300 . . . . . 200. . . . . . . N.A. Tail : < 100. . . . . . .100 . . . . 100 . . . . . . . 100 Fluid Loss Control Chevron DTC
  • 73. Calculating Pressure to Reverse-Out Always know what pressures are required to reverse-out. Step 1: Calculate Differential Fluid Gradient, psi/ft 15.6 ppg x 0.052 = 0.8112 psi/ft ( Cement ) 10.0 ppg x 0.052 = 0.5200 psi/ft ( Comp Fluid ) 0.2912 psi/ft Step II: Determine Tubing Fill Factor, ft/bbl (decimal book) 2-3/8” 4.7 lbs/ft tubing = 258.65 ft/bbl of fill Step III: Calculate Pressure to Reverse-Out, psi/bbl ex: 258.65 ft/bbl x 0.2912 psi/ft = 75.3 psi/bbl* *Multiple psi/bbl by the barrels of slurry left in the tubing
  • 74. Hesitation Squeeze Final squeeze is achieved when the leak-off becomes negligible For loose, permeable formations a first hesitation period of up to 30 minutes is not unreasonable For tight low permeability formations a short first hesitation period of ± 5 minutes is sufficient
  • 75. Hesitation Squeeze (Chevron DTC) Always Test on Hesitation Schedule Hesitation Time Dictated by Pressure Build-up Be Patient Use CFL Slurry Know the Location of the Cement Never Over-Displace Determine Final Squeeze Pressure from Injection Profile
  • 76. Misconceptions of Squeeze Cementing Cement slurry enters formation pore spaces All perforations are open High pressure squeezes create horizontal pancake High final pressure is required to assure success Final squeeze pressure must equal future working pressure
  • 77. General Recommendations Ensure hole is junk free Ensure perforations are open Acid wash if necessary Low pressure squeeze where possible Use low fluid loss cement Cement volume should not exceed string volume High final squeeze pressure is not essential Batch mix cement Allow adequate time for cement to set based on compressive strength data

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