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ARTIFICIAL LIFT TECHNOLOGYARTIFICIAL LIFT TECHNOLOGY
Oil Field Production Phases
The production of crude oil in oil
reservoirs can include up to three distinct
phases: primary, secondary, and tertiary
recovery.
During primary recovery, the natural
pressure of the reservoir, combined with
pumping equipment, brings oil to the
surface. Primary recovery is the easiest
and cheapest way to extract oil from the
ground. But this method of production
typically produces only about 10 percent
of a reservoir's original oil in place
reserve.
Oil Field Production Phases
In the secondary recovery phase, water or gas is
injected to displace oil, making it much easier to
drive it to a production well bore.
This technique generally results in the recovery
of 20 to 40 percent of the original oil in place.
Oil Field Production Phases
When companies talk about enhanced
oil recovery, they're really referring to
the tertiary recovery phase. Tertiary
recovery involves injecting other gases,
such as carbon dioxide, to stimulate the
flow of the oil and to produce remaining
fluids that were not extracted during
primary or secondary recovery phases.
Oil Field Production Phases
These methods are not used routinely because
they are expensive. When the price of oil
increases, there is greater incentive to use them
and thus increase, to some degree, the proven
reserves of oil.
The amount of oil that is recoverable is
determined by a number of factors including the
permeability of the rocks, the strength of natural
drives (the gas present, pressure from adjacent
water or gravity), and the viscosity of the oil.
Producing The Well
Because oil, gas and water in underground are
under a lot of pressure at first, these fluids flow
up a wellbore all by themselves, much like a soft
drink that has been shaken up. When oil and
gas are produced this way, it is called primary
recovery.
Artificial lift is installed in wells that:
i) Do not have sufficient reservoir pressure to
raise fluids to surface
ii) Need to supplement the natural reservoir
drive in boosting fluids out of the wellbore.
MODES OF ARTIFICIAL LIFT
Reciprocating Rod Lift Systems
Progressing Cavity Pumping Systems
Hydraulic Lift Systems
Gas Lift Systems
Plunger Lift Systems
Electric Submersible Pumping Systems
Selection Parameters
Well Completion & profile
Geographical & Environmental conditions
Reservoir characteristics
Reservoir pressure & Well productivity
Characteristics of fluids
Surface Constraints
Services available
Economic considerations
Operating ease
Gas Lift
ESP’s
PC Pumps
Hydraulic
Pumps
Beam pump
ARTIFICIAL LIFT METHODS
Artificial-lift in Assam Asset
Reciprocating Rod Lift Systems
Pumping Units
Motors & Controls
Continuous & Threaded
Sucker Rods
Rod Pumps &Accessories
Pumping Unit Services
Reciprocating Rod Lift
System Advantages
High System Efficiency
Optimization Controls Available
Economical to Repair and Service
Positive Displacement/Strong
Drawdown
Upgraded Materials Reduce
Corrosion Concerns
Flexibility - Adjust Production
Through Stroke Length and Speed
High Salvage Value for Surface &
Downhole Equipment
Sucker Rod
Tubing Anchor/
Catcher
Sucker Rod
Pump
Assembly
Potential for Tubing and Rod Wear
Gas-Oil Ratios
Most Systems Limited to Ability of
Rods to Handle Loads
( Volume Decreases As Depth Increases)
Environmental and Aesthetic
Concerns
Reciprocating Rod Lift
System Limitations
Sucker Rod
Tubing Anchor/
Catcher
Sucker Rod
Pump
Assembly
Rod Lift System Application Considerations
Typical Range Maximum*
Operating
Depth 100 - 11,000’ TVD 16,000’ TVD
Operating
Volume 5 - 1500 BPD 5000 BPD
Operating
Temperature 100° - 350° F 550° F
Wellbore 0 - 20° Landed 0 - 90° Landed
Deviation Pump Pump -
<15°/100’
Build Angle
Corrosion Handling Good to Excellent
w/ Upgraded Materials
Gas Handling Fair to Good
Solids Handling Fair to Good
Fluid Gravity >8° API
Servicing Work over or Pulling Rig
Prime Mover Type Gas or Electric
Offshore Application Limited
System Efficiency 45%-60%
*Special
Analysis
Required
Sucker Rod
Tubing Anchor/
Catcher
Sucker Rod
Pump
Assembly
Progressing Cavity Pumping Systems
Wellhead Surface Drives
Continuous & Threaded Sucker Rods
Subsurface PC Pumps & Accessories
Stator
Vertical
Electric Wellhead
Drive
Casing
Production Tubing
Sucker Rod
Sucker Rod Coupling
Tubing Collar
Rotor
Tubing Collar
Tag Bar Sub
Progressing Cavity
Pumping System
Advantages
Low Capital Cost
Low Surface Profile for Visual & Height
Sensitive Areas
High System Efficiency
Simple Installation, Quiet Operation
Pumps Oils and Waters with Solids
Low Power Consumption
Portable Surface Equipment
Low Maintenance Costs
Use In Horizontal/Directional Wells
Limited Depth Capability
Temperature
Sensitivity to Produced Fluids
Low Volumetric Efficiencies in
High-Gas Environments
Potential for Tubing and Rod
Coupling Wear
Requires Constant Fluid Level above
Pump
Progressing Cavity Pumping
System LimitationsVertical
Electric Wellhead
Drive
Casing
Production Tubing
Sucker Rod
Sucker Rod Coupling
Tubing Collar
Stator
Rotor
Tubing Collar
Tag Bar Sub
Progressing Cavity System Application
ConsiderationsTypical Range Maximum*
Operating
Depth 2,000 --4,500’ TVD 6,000’ TVD
Operating
Volume 5 - 2,200 BPD 4,500 BPD
Operating
Temperature 75 -150° F 250° F
Wellbore N/A 0 - 90° Landed
Deviation Pump -
<15°/100’
Build Angle
Corrosion Handling Fair
Gas Handling Good
Solids Handling Excellent
Fluid Gravity <35° API
Servicing Workover or Pulling Rig
Prime Mover Type Gas or Electric
Offshore Application Good (ES/PCP)
System Efficiency 40%-70%
*Special
Analysis
Required
Vertical
Electric Wellhead
Drive
Casing
Production Tubing
Sucker Rod
Sucker Rod Coupling
Tubing Collar
Stator
Rotor
Tubing Collar
Tag Bar Sub
Gas Lift Systems
Gas Lift Valves
Mandrels
Latches
Kick over Tools
Surface Controls
Coiled-Tubing
Gas Lift Equipment
Pack-Off Equipment
Gas Lift
System Advantages
High Degree of Flexibility and Design Rates
Wireline Retrievable
Handles Sandy Conditions Well
Allows For Full Bore Tubing Drift
Surface Wellhead Equipment Requires Minimal Space
Multi-Well Production From Single Compressor
Multiple or Slim hole Completion
Produced
Hydrocarbons
Out
Injection
Gas In
Side Pocket
Mandrel with
Gas Lift Valve
Completion
Fluid
Side Pocket
Mandrel with
Gas Lift Valve
Single Production
Packer
Side Pocket
Mandrel with
Gas Lift Valve
Needs High-Pressure Gas Well or Compressor
One Well Leases May Be Uneconomical
Fluid Viscosity
Bottom hole Pressure
High Back-Pressure
Gas Lift
System LimitationsProduced
Hydrocarbons
Out
Injection
Gas In
Side Pocket
Mandrel with
Gas Lift Valve
Completion
Fluid
Side Pocket
Mandrel with
Gas Lift Valve
Single Production
Packer
Side Pocket
Mandrel with
Gas Lift Valve
Gas Lift System Application Considerations
Typical Range Maximum*
Operating
Depth 5,000 -10,000’ TVD 15,000’ TVD
Operating
Volume 100 - 10,000 BPD 30,000 BPD
Operating
Temperature 100 - 250° F 400° F
Wellbore 0- 50° 70°
Deviation Short to
Medium
Radius
Corrosion Handling Good to Excellent with
Upgraded Materials
Gas Handling Excellent
Solids Handling Good
Fluid Gravity Best in >15° API
Servicing Wireline or Work over Rig
Prime Mover Type Compressor
Offshore Application Excellent
System Efficiency 10% - 30%
*Special
Analysis
Required
Produced
Hydrocarbons
Out
Injection
Gas In
Side Pocket
Mandrel with
Gas Lift Valve
Completion
Fluid
Side Pocket
Mandrel with
Gas Lift Valve
Single
Production
Packer
Side Pocket
Mandrel with
Gas Lift Valve
Plunger Lift Systems
Lubricators
Plungers
Bumper Springs
Controllers
Accessories
Plunger Lift
System Advantages
Requires No Outside Energy Source -
Uses Well’s Energy to Lift
Dewatering Gas Wells
Rig Not Required for Installation
Easy Maintenance
Keeps Well Cleaned of Paraffin Deposits
Low Cost Artificial Lift Method
Handles Gassy Wells
Good in Deviated Wells
Can Produce Well to Depletion
Lubricator
Catcher
Orifice Control
Valves
Solar Panel
Controller
Motor Valve
Dual “T” Pad
Plunger
Bumper
Spring
Specific GLR’s to Drive System
Low Volume Potential (200 BPD)
Solids
Requires Surveillance to Optimize
Plunger Lift
System Limitations
Lubricator
Catcher
Orifice Control
Valves
Solar Panel
Controller
Motor Valve
Dual “T” Pad
Plunger
Bumper
Spring
Plunger Lift System Application
Considerations
Typical Range Maximum*
Operating
Depth 8,000’ TVD 19,000’ TVD
Operating
Volume 1-5 BPD 200 BPD
Operating
Temperature 120° F 500° F
Wellbore N/A 80°
Deviation
Corrosion Handling Excellent
Gas Handling Excellent
Solids Handling Poor to Fair
GLR Required 300 SCF/BBL/1000’ Depth
Servicing Wellhead Catcher or Wireline
Prime Mover Type Well’s Natural Energy
Offshore Application N/A at this time
System Efficiency N/A
*Special
Analysis
Required
Orifice Control
Valves
Solar Panel
Controller
Motor Valve
Dual “T” Pad
Plunger
Bumper
Spring
Lubricator
Catcher
Hydraulic Lift Systems
Surface Hydraulic Equipment
Jet Pumps
Hydraulic Jet Lift System
Advantages
No Moving Parts
High Volume Capability
“Free” Pump
Deviated Wells
Multi-Well Production from
Single Surface Package
Low Pump Maintenance
Production
Casing
High Pressure
Power Fluid
Packer Nose
Bottom Hole
Assembly
Piston or Jet
“Free Pump”
Standing Valve
Surface Power
Fluid Package
Producing Rate Relative to Bottomhole Pressure
Some Require Specific Bottomhole Assemblies
Lower Horsepower Efficiency
High-Pressure Surface Line Requirements
Hydraulic Jet Lift System
Limitations
Production
Casing
High Pressure
Power Fluid
Packer Nose
Bottom Hole
Assembly
Piston or Jet
“Free Pump”
Standing Valve
Surface Power
Fluid Package
Hydraulic Jet Lift Application Considerations
Typical Range Maximum*
Operating
Depth 5,000 - 10,000’ TVD 15,000’ TVD
Operating
Volume 300 - 1,000 BPD >15,000 BPD
Operating
Temperature 100° - 250° F 500° F
Wellbore 0 - 20° 0 - 90° Pump
Deviation Hole Angle Placement -
<24°/100’
Build Angle
Corrosion Handling Excellent
Gas Handling Good
Solids Handling Good
Fluid Gravity >8° API
Servicing Hydraulic or Wireline
Prime Mover Type Multi-Cylinder or Electric
Offshore Application Excellent
System Efficiency 10%-30%
*Special
Analysis
Required
Surface Power
Fluid Package
Production
Casing
High Pressure
Power Fluid
Packer Nose
Bottom Hole
Assembly
Piston or Jet
“Free Pump”
Standing Valve
Electric Submersible
Pumping Systems
Wellhead Equipment
Power Cables
Pumps & Motors
Variable Speed Drives
Gas Separators
Electric Submersible
Pumping System
Advantages
High Volume and Depth Capability
High Efficiency Over 1,000 BPD
Low Maintenance
Minor Surface Equipment Needs
Good in Deviated Wells
Adaptable in Casings > 4-1/2”
Use for Well Testing
Vent Box
Motor Control
Pump
Seal Section
Motor
Production
Tubing
Produced
Hydrocarbons Out
Flat Cable
Extension
Available Electric Power
Limited Adaptability to Major Changes in
Reservoir
Difficult to Repair In the Field
Free Gas and/or Abrasives
High Viscosity
Higher Pulling Costs
Electric Submersible
Pumping System
Limitations
Vent Box
Motor Control
Pump
Seal Section
Motor
Production
Tubing
Produced
Hydrocarbons Out
Flat Cable
Extension
Electric Submersible Systems Application
Considerations
Typical Range Maximum*
Operating
Depth 1,000’ - 10,000’ TVD 15,000’ TVD
Operating
Volume 200 - 20,000 BPD 30,000 BPD
Operating
Temperature 100° - 275° F 400° F
Wellbore 10° 0 - 90° Pump
Deviation Placement -
<10° Build
Angle
Corrosion Handling Good
Gas Handling Poor to Fair
Solids Handling Poor to Fair
Fluid Gravity >10° API
Servicing Workover or Pulling Rig
Prime Mover Type Electric Motor
Offshore Application Excellent
System Efficiency 35%-60%
*Special
Analysis
Required
Vent Box
Motor Control
Pump
Seal Section
Motor
Production
Tubing
Produced
Hydrocarbons Out
Flat Cable
Extension
Wellsite Optimization Equipment
Remote Communication
Packages
Data Gathering Systems
Lift System Selection – How to
Approach
Do more than —
merely offer every type of major lift system.merely offer every type of major lift system.
Provide —
smart solutions for enhanced production.smart solutions for enhanced production.
This means—
systematic evaluations to ensure the final
solution is one that provides the
highest return on your investment.
systematic evaluations to ensure the final
solution is one that provides the
highest return on your investment.
Artificial Lift Selection
Project ScopeProject Scope1.1.
Systems AnalysisSystems Analysis3.3.
Final SelectionFinal Selection4.4.
Follow-Up AnalysisFollow-Up Analysis5.5.
Elimination ProcessElimination Process2.2.
Project ScopeProject Scope1.1.
General Field Requirements
Data Collection
Data Confirmation
Project ScopeProject Scope1.1.
Well Information
Production & Fluid Information
Desired Production Rate
System Details
Data Collection/Confirmation
Easy Eliminations
More Detailed Reviews
Applicable Systems
Elimination ProcessElimination Process2.2.
Selection Process
Operating
Depth
Operating
Volume (Typical)
Operating
Temperature
Corrosion
Handling
Gas
Handling
Solids
Handling
Fluid
Gravity
Servicing
Prime Mover
Offshore
Application
Overall System
Efficiency
Rod Lift Progressing
Cavity
Gas Lift Plunger
Lift
Hydraulic
Piston
Hydraulic
Jet
100’ -
16,000’ TVD
5 - 5000
BPD
100° -
550° F
Good to
Excellent
Fair to
Good
Fair to
Good
>8° API
Work over or
Pulling Rig
Gas or
Electric
Limited
45% - 60%
2,000’ -
6,000’ TVD
5 - 4,500
BPD
75°-250° F
Fair
Good
Excellent
<35° API
Work over
or
Pulling Rig
Gas or
Electric
Good
40% - 70%
7,500’ -
17,000’ TVD
50 - 4,000
BPD
100° -
500° F
Good
Fair
Poor
>8° API
Hydraulic or
Wireline
Multicylinder
or Electric
Good
45% - 55%
5,000’ -
15,000’ TVD
300 - >15,000
BPD
100° -
500° F
Excellent
Good
Good
>8° API
Hydraulic or
Wireline
Multicylinder
or Electric
Excellent
10% - 30%
5,000’ -
15,000’ TVD
200 - 30,000
BPD
100° -
400° F
Excellent
Good
>15° API
Wireline or
Work over
Rig
Compressor
Excellent
10% - 30%
8,000’ -
19,000’ TVD
1 - 5 BPD
120° -
500º F
Excellent
Excellent
Poor to
Fair
Wellhead
Catcher or Wireline
Wells’ Natural
Energy
N/A
N/A
GLR Required -
300 SCF/BBL/
1000’ Depth
Electric
Motor
100° -
400° F
Good
Poor to
Fair
Poor
to Fair
>10° API
Workover or
Pulling Rig
Excellent
35% - 60%
1,000’-
15,000’ TVD
200 - 30,000
BPD
Good to
Excellent
Electric
Submersible
Elimination ProcessElimination Process2.2.
Performance Comparison
Characteristic SRP PCP ESP Gas Lift Jet
Rates Poor Fair Good Excellent Good
Gas Production Fair Poor Poor Excellent Good
Viscous Fluids Good Excellent Fair Fair Excellent
Emulsions Good Excellent Fair Fair Excellent
Solid Handling Fair Fair Poor Excellent Excellent
Wax Mitigation Fair Fair Fair Good Excellent
Corrosion Good Good Fair Good Excellent
Reliability Excellent Good Varies Excellent Good
Efficiency Good Good Fair Poor Poor
Capital Costs Moderate Low Moderate Moderate Moderate
Operating Costs Low Low High Low Moderate
Elimination ProcessElimination Process2.2.
SPE 59026
Elimination ProcessElimination Process2.2.
High
Volume
Hydraulic
Jet Pumps,
Electric
Submersible
Pumping
and Gas Lift
35,000
30,000
25,000
20,000
15,000
10,000
5,000
1,000
2,000
3,000
4,000
5,000
6,000
7,000
8,000
9,000
10,000
11,000
12,000
13,000
14,000
15,000
16,000
Gas LiftESP
Hydraulic
Jet Pump
BarrelsperDay
Lift Depth
Elimination ProcessElimination Process2.2.
500
1,000
1,500
2,000
2,500
3,000
3,500
4,000
4,500
1,000
2,000
3,000
4,000
5,000
6,000
7,000
8,000
9,000
10,000
11,000
12,000
13,000
14,000
15,000
16,000
Recip. Hydraulic
Recip. Rod Pump
PC Pumps
Plunger Lift
BarrelsperDay
Lift Depth
Lower
Volume
Reciprocating
Hydraulic
Pumps,
PC Pumps,
Rod Pumps &
Plunger Lift
Elimination ProcessElimination Process2.2.
Systems AnalysisSystems AnalysisSystems Analysis3.3.
Selection Process
ESP SubPUMP,PROPSER
Reciprocating Rod Lift Rod Star, NABLA,
API Rod, Tamer
PCP C-Fer
Gas Lift PROSPER, PIPESIM,GLIDE
Hydraulic Jet 4.1, Super H &
Pump Eval
Type Lift Programs
Proposal for Viable Forms of Lift
Economic Evaluation Model
- Capital Expenditure
- Operating Expenses
- Comprehensive Analysis
What Equipment is Available?
Selection Process
Final SelectionFinal Selection4.4.
Final SelectionFinal Selection4.4.
Cost Category
Rod
Lift
“CAPEX”
Installation Cost
Energy Cost Per
Month
Failure Frequency
Equipment Repair
$/Failure
Well Service Cost
$/Failure
PCP
Plunger
Lift
Gas
Lift
Hydr.
Piston
Hydr.
Jet
ESP
“OPEX” Annual
Total $
CAPEX / OPEX SUMMARY*CAPEX / OPEX SUMMARY*
Did System Meet Expectations?
Continuous Process of Evaluation
and Follow-Up on Failure Rates,
Confirm Costs, etc.
Follow-Up AnalysisFollow-Up Analysis5.5.

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Artificial lift technology

  • 2. Oil Field Production Phases The production of crude oil in oil reservoirs can include up to three distinct phases: primary, secondary, and tertiary recovery. During primary recovery, the natural pressure of the reservoir, combined with pumping equipment, brings oil to the surface. Primary recovery is the easiest and cheapest way to extract oil from the ground. But this method of production typically produces only about 10 percent of a reservoir's original oil in place reserve.
  • 3. Oil Field Production Phases In the secondary recovery phase, water or gas is injected to displace oil, making it much easier to drive it to a production well bore. This technique generally results in the recovery of 20 to 40 percent of the original oil in place.
  • 4. Oil Field Production Phases When companies talk about enhanced oil recovery, they're really referring to the tertiary recovery phase. Tertiary recovery involves injecting other gases, such as carbon dioxide, to stimulate the flow of the oil and to produce remaining fluids that were not extracted during primary or secondary recovery phases.
  • 5. Oil Field Production Phases These methods are not used routinely because they are expensive. When the price of oil increases, there is greater incentive to use them and thus increase, to some degree, the proven reserves of oil. The amount of oil that is recoverable is determined by a number of factors including the permeability of the rocks, the strength of natural drives (the gas present, pressure from adjacent water or gravity), and the viscosity of the oil.
  • 6. Producing The Well Because oil, gas and water in underground are under a lot of pressure at first, these fluids flow up a wellbore all by themselves, much like a soft drink that has been shaken up. When oil and gas are produced this way, it is called primary recovery. Artificial lift is installed in wells that: i) Do not have sufficient reservoir pressure to raise fluids to surface ii) Need to supplement the natural reservoir drive in boosting fluids out of the wellbore.
  • 7. MODES OF ARTIFICIAL LIFT Reciprocating Rod Lift Systems Progressing Cavity Pumping Systems Hydraulic Lift Systems Gas Lift Systems Plunger Lift Systems Electric Submersible Pumping Systems
  • 8. Selection Parameters Well Completion & profile Geographical & Environmental conditions Reservoir characteristics Reservoir pressure & Well productivity Characteristics of fluids Surface Constraints Services available Economic considerations Operating ease
  • 9. Gas Lift ESP’s PC Pumps Hydraulic Pumps Beam pump ARTIFICIAL LIFT METHODS
  • 11. Reciprocating Rod Lift Systems Pumping Units Motors & Controls Continuous & Threaded Sucker Rods Rod Pumps &Accessories Pumping Unit Services
  • 12.
  • 13. Reciprocating Rod Lift System Advantages High System Efficiency Optimization Controls Available Economical to Repair and Service Positive Displacement/Strong Drawdown Upgraded Materials Reduce Corrosion Concerns Flexibility - Adjust Production Through Stroke Length and Speed High Salvage Value for Surface & Downhole Equipment Sucker Rod Tubing Anchor/ Catcher Sucker Rod Pump Assembly
  • 14. Potential for Tubing and Rod Wear Gas-Oil Ratios Most Systems Limited to Ability of Rods to Handle Loads ( Volume Decreases As Depth Increases) Environmental and Aesthetic Concerns Reciprocating Rod Lift System Limitations Sucker Rod Tubing Anchor/ Catcher Sucker Rod Pump Assembly
  • 15. Rod Lift System Application Considerations Typical Range Maximum* Operating Depth 100 - 11,000’ TVD 16,000’ TVD Operating Volume 5 - 1500 BPD 5000 BPD Operating Temperature 100° - 350° F 550° F Wellbore 0 - 20° Landed 0 - 90° Landed Deviation Pump Pump - <15°/100’ Build Angle Corrosion Handling Good to Excellent w/ Upgraded Materials Gas Handling Fair to Good Solids Handling Fair to Good Fluid Gravity >8° API Servicing Work over or Pulling Rig Prime Mover Type Gas or Electric Offshore Application Limited System Efficiency 45%-60% *Special Analysis Required Sucker Rod Tubing Anchor/ Catcher Sucker Rod Pump Assembly
  • 16. Progressing Cavity Pumping Systems Wellhead Surface Drives Continuous & Threaded Sucker Rods Subsurface PC Pumps & Accessories
  • 17. Stator Vertical Electric Wellhead Drive Casing Production Tubing Sucker Rod Sucker Rod Coupling Tubing Collar Rotor Tubing Collar Tag Bar Sub Progressing Cavity Pumping System Advantages Low Capital Cost Low Surface Profile for Visual & Height Sensitive Areas High System Efficiency Simple Installation, Quiet Operation Pumps Oils and Waters with Solids Low Power Consumption Portable Surface Equipment Low Maintenance Costs Use In Horizontal/Directional Wells
  • 18. Limited Depth Capability Temperature Sensitivity to Produced Fluids Low Volumetric Efficiencies in High-Gas Environments Potential for Tubing and Rod Coupling Wear Requires Constant Fluid Level above Pump Progressing Cavity Pumping System LimitationsVertical Electric Wellhead Drive Casing Production Tubing Sucker Rod Sucker Rod Coupling Tubing Collar Stator Rotor Tubing Collar Tag Bar Sub
  • 19. Progressing Cavity System Application ConsiderationsTypical Range Maximum* Operating Depth 2,000 --4,500’ TVD 6,000’ TVD Operating Volume 5 - 2,200 BPD 4,500 BPD Operating Temperature 75 -150° F 250° F Wellbore N/A 0 - 90° Landed Deviation Pump - <15°/100’ Build Angle Corrosion Handling Fair Gas Handling Good Solids Handling Excellent Fluid Gravity <35° API Servicing Workover or Pulling Rig Prime Mover Type Gas or Electric Offshore Application Good (ES/PCP) System Efficiency 40%-70% *Special Analysis Required Vertical Electric Wellhead Drive Casing Production Tubing Sucker Rod Sucker Rod Coupling Tubing Collar Stator Rotor Tubing Collar Tag Bar Sub
  • 20. Gas Lift Systems Gas Lift Valves Mandrels Latches Kick over Tools Surface Controls Coiled-Tubing Gas Lift Equipment Pack-Off Equipment
  • 21.
  • 22. Gas Lift System Advantages High Degree of Flexibility and Design Rates Wireline Retrievable Handles Sandy Conditions Well Allows For Full Bore Tubing Drift Surface Wellhead Equipment Requires Minimal Space Multi-Well Production From Single Compressor Multiple or Slim hole Completion Produced Hydrocarbons Out Injection Gas In Side Pocket Mandrel with Gas Lift Valve Completion Fluid Side Pocket Mandrel with Gas Lift Valve Single Production Packer Side Pocket Mandrel with Gas Lift Valve
  • 23. Needs High-Pressure Gas Well or Compressor One Well Leases May Be Uneconomical Fluid Viscosity Bottom hole Pressure High Back-Pressure Gas Lift System LimitationsProduced Hydrocarbons Out Injection Gas In Side Pocket Mandrel with Gas Lift Valve Completion Fluid Side Pocket Mandrel with Gas Lift Valve Single Production Packer Side Pocket Mandrel with Gas Lift Valve
  • 24. Gas Lift System Application Considerations Typical Range Maximum* Operating Depth 5,000 -10,000’ TVD 15,000’ TVD Operating Volume 100 - 10,000 BPD 30,000 BPD Operating Temperature 100 - 250° F 400° F Wellbore 0- 50° 70° Deviation Short to Medium Radius Corrosion Handling Good to Excellent with Upgraded Materials Gas Handling Excellent Solids Handling Good Fluid Gravity Best in >15° API Servicing Wireline or Work over Rig Prime Mover Type Compressor Offshore Application Excellent System Efficiency 10% - 30% *Special Analysis Required Produced Hydrocarbons Out Injection Gas In Side Pocket Mandrel with Gas Lift Valve Completion Fluid Side Pocket Mandrel with Gas Lift Valve Single Production Packer Side Pocket Mandrel with Gas Lift Valve
  • 25. Plunger Lift Systems Lubricators Plungers Bumper Springs Controllers Accessories
  • 26. Plunger Lift System Advantages Requires No Outside Energy Source - Uses Well’s Energy to Lift Dewatering Gas Wells Rig Not Required for Installation Easy Maintenance Keeps Well Cleaned of Paraffin Deposits Low Cost Artificial Lift Method Handles Gassy Wells Good in Deviated Wells Can Produce Well to Depletion Lubricator Catcher Orifice Control Valves Solar Panel Controller Motor Valve Dual “T” Pad Plunger Bumper Spring
  • 27. Specific GLR’s to Drive System Low Volume Potential (200 BPD) Solids Requires Surveillance to Optimize Plunger Lift System Limitations Lubricator Catcher Orifice Control Valves Solar Panel Controller Motor Valve Dual “T” Pad Plunger Bumper Spring
  • 28. Plunger Lift System Application Considerations Typical Range Maximum* Operating Depth 8,000’ TVD 19,000’ TVD Operating Volume 1-5 BPD 200 BPD Operating Temperature 120° F 500° F Wellbore N/A 80° Deviation Corrosion Handling Excellent Gas Handling Excellent Solids Handling Poor to Fair GLR Required 300 SCF/BBL/1000’ Depth Servicing Wellhead Catcher or Wireline Prime Mover Type Well’s Natural Energy Offshore Application N/A at this time System Efficiency N/A *Special Analysis Required Orifice Control Valves Solar Panel Controller Motor Valve Dual “T” Pad Plunger Bumper Spring Lubricator Catcher
  • 29. Hydraulic Lift Systems Surface Hydraulic Equipment Jet Pumps
  • 30. Hydraulic Jet Lift System Advantages No Moving Parts High Volume Capability “Free” Pump Deviated Wells Multi-Well Production from Single Surface Package Low Pump Maintenance Production Casing High Pressure Power Fluid Packer Nose Bottom Hole Assembly Piston or Jet “Free Pump” Standing Valve Surface Power Fluid Package
  • 31. Producing Rate Relative to Bottomhole Pressure Some Require Specific Bottomhole Assemblies Lower Horsepower Efficiency High-Pressure Surface Line Requirements Hydraulic Jet Lift System Limitations Production Casing High Pressure Power Fluid Packer Nose Bottom Hole Assembly Piston or Jet “Free Pump” Standing Valve Surface Power Fluid Package
  • 32. Hydraulic Jet Lift Application Considerations Typical Range Maximum* Operating Depth 5,000 - 10,000’ TVD 15,000’ TVD Operating Volume 300 - 1,000 BPD >15,000 BPD Operating Temperature 100° - 250° F 500° F Wellbore 0 - 20° 0 - 90° Pump Deviation Hole Angle Placement - <24°/100’ Build Angle Corrosion Handling Excellent Gas Handling Good Solids Handling Good Fluid Gravity >8° API Servicing Hydraulic or Wireline Prime Mover Type Multi-Cylinder or Electric Offshore Application Excellent System Efficiency 10%-30% *Special Analysis Required Surface Power Fluid Package Production Casing High Pressure Power Fluid Packer Nose Bottom Hole Assembly Piston or Jet “Free Pump” Standing Valve
  • 33. Electric Submersible Pumping Systems Wellhead Equipment Power Cables Pumps & Motors Variable Speed Drives Gas Separators
  • 34. Electric Submersible Pumping System Advantages High Volume and Depth Capability High Efficiency Over 1,000 BPD Low Maintenance Minor Surface Equipment Needs Good in Deviated Wells Adaptable in Casings > 4-1/2” Use for Well Testing Vent Box Motor Control Pump Seal Section Motor Production Tubing Produced Hydrocarbons Out Flat Cable Extension
  • 35. Available Electric Power Limited Adaptability to Major Changes in Reservoir Difficult to Repair In the Field Free Gas and/or Abrasives High Viscosity Higher Pulling Costs Electric Submersible Pumping System Limitations Vent Box Motor Control Pump Seal Section Motor Production Tubing Produced Hydrocarbons Out Flat Cable Extension
  • 36. Electric Submersible Systems Application Considerations Typical Range Maximum* Operating Depth 1,000’ - 10,000’ TVD 15,000’ TVD Operating Volume 200 - 20,000 BPD 30,000 BPD Operating Temperature 100° - 275° F 400° F Wellbore 10° 0 - 90° Pump Deviation Placement - <10° Build Angle Corrosion Handling Good Gas Handling Poor to Fair Solids Handling Poor to Fair Fluid Gravity >10° API Servicing Workover or Pulling Rig Prime Mover Type Electric Motor Offshore Application Excellent System Efficiency 35%-60% *Special Analysis Required Vent Box Motor Control Pump Seal Section Motor Production Tubing Produced Hydrocarbons Out Flat Cable Extension
  • 37. Wellsite Optimization Equipment Remote Communication Packages Data Gathering Systems
  • 38. Lift System Selection – How to Approach Do more than — merely offer every type of major lift system.merely offer every type of major lift system. Provide — smart solutions for enhanced production.smart solutions for enhanced production. This means— systematic evaluations to ensure the final solution is one that provides the highest return on your investment. systematic evaluations to ensure the final solution is one that provides the highest return on your investment.
  • 39.
  • 40. Artificial Lift Selection Project ScopeProject Scope1.1. Systems AnalysisSystems Analysis3.3. Final SelectionFinal Selection4.4. Follow-Up AnalysisFollow-Up Analysis5.5. Elimination ProcessElimination Process2.2.
  • 41. Project ScopeProject Scope1.1. General Field Requirements Data Collection Data Confirmation
  • 42. Project ScopeProject Scope1.1. Well Information Production & Fluid Information Desired Production Rate System Details Data Collection/Confirmation
  • 43. Easy Eliminations More Detailed Reviews Applicable Systems Elimination ProcessElimination Process2.2. Selection Process
  • 44. Operating Depth Operating Volume (Typical) Operating Temperature Corrosion Handling Gas Handling Solids Handling Fluid Gravity Servicing Prime Mover Offshore Application Overall System Efficiency Rod Lift Progressing Cavity Gas Lift Plunger Lift Hydraulic Piston Hydraulic Jet 100’ - 16,000’ TVD 5 - 5000 BPD 100° - 550° F Good to Excellent Fair to Good Fair to Good >8° API Work over or Pulling Rig Gas or Electric Limited 45% - 60% 2,000’ - 6,000’ TVD 5 - 4,500 BPD 75°-250° F Fair Good Excellent <35° API Work over or Pulling Rig Gas or Electric Good 40% - 70% 7,500’ - 17,000’ TVD 50 - 4,000 BPD 100° - 500° F Good Fair Poor >8° API Hydraulic or Wireline Multicylinder or Electric Good 45% - 55% 5,000’ - 15,000’ TVD 300 - >15,000 BPD 100° - 500° F Excellent Good Good >8° API Hydraulic or Wireline Multicylinder or Electric Excellent 10% - 30% 5,000’ - 15,000’ TVD 200 - 30,000 BPD 100° - 400° F Excellent Good >15° API Wireline or Work over Rig Compressor Excellent 10% - 30% 8,000’ - 19,000’ TVD 1 - 5 BPD 120° - 500º F Excellent Excellent Poor to Fair Wellhead Catcher or Wireline Wells’ Natural Energy N/A N/A GLR Required - 300 SCF/BBL/ 1000’ Depth Electric Motor 100° - 400° F Good Poor to Fair Poor to Fair >10° API Workover or Pulling Rig Excellent 35% - 60% 1,000’- 15,000’ TVD 200 - 30,000 BPD Good to Excellent Electric Submersible Elimination ProcessElimination Process2.2.
  • 45. Performance Comparison Characteristic SRP PCP ESP Gas Lift Jet Rates Poor Fair Good Excellent Good Gas Production Fair Poor Poor Excellent Good Viscous Fluids Good Excellent Fair Fair Excellent Emulsions Good Excellent Fair Fair Excellent Solid Handling Fair Fair Poor Excellent Excellent Wax Mitigation Fair Fair Fair Good Excellent Corrosion Good Good Fair Good Excellent Reliability Excellent Good Varies Excellent Good Efficiency Good Good Fair Poor Poor Capital Costs Moderate Low Moderate Moderate Moderate Operating Costs Low Low High Low Moderate Elimination ProcessElimination Process2.2.
  • 47. High Volume Hydraulic Jet Pumps, Electric Submersible Pumping and Gas Lift 35,000 30,000 25,000 20,000 15,000 10,000 5,000 1,000 2,000 3,000 4,000 5,000 6,000 7,000 8,000 9,000 10,000 11,000 12,000 13,000 14,000 15,000 16,000 Gas LiftESP Hydraulic Jet Pump BarrelsperDay Lift Depth Elimination ProcessElimination Process2.2.
  • 48. 500 1,000 1,500 2,000 2,500 3,000 3,500 4,000 4,500 1,000 2,000 3,000 4,000 5,000 6,000 7,000 8,000 9,000 10,000 11,000 12,000 13,000 14,000 15,000 16,000 Recip. Hydraulic Recip. Rod Pump PC Pumps Plunger Lift BarrelsperDay Lift Depth Lower Volume Reciprocating Hydraulic Pumps, PC Pumps, Rod Pumps & Plunger Lift Elimination ProcessElimination Process2.2.
  • 49. Systems AnalysisSystems AnalysisSystems Analysis3.3. Selection Process ESP SubPUMP,PROPSER Reciprocating Rod Lift Rod Star, NABLA, API Rod, Tamer PCP C-Fer Gas Lift PROSPER, PIPESIM,GLIDE Hydraulic Jet 4.1, Super H & Pump Eval Type Lift Programs
  • 50. Proposal for Viable Forms of Lift Economic Evaluation Model - Capital Expenditure - Operating Expenses - Comprehensive Analysis What Equipment is Available? Selection Process Final SelectionFinal Selection4.4.
  • 51. Final SelectionFinal Selection4.4. Cost Category Rod Lift “CAPEX” Installation Cost Energy Cost Per Month Failure Frequency Equipment Repair $/Failure Well Service Cost $/Failure PCP Plunger Lift Gas Lift Hydr. Piston Hydr. Jet ESP “OPEX” Annual Total $ CAPEX / OPEX SUMMARY*CAPEX / OPEX SUMMARY*
  • 52. Did System Meet Expectations? Continuous Process of Evaluation and Follow-Up on Failure Rates, Confirm Costs, etc. Follow-Up AnalysisFollow-Up Analysis5.5.