Carbon Dioxide Demonstration Project Supporting Research at KU - PowerPoint PPT Presentation

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Carbon Dioxide Demonstration Project Supporting Research at KU

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Equation of state (EOS) for CO2-oil phase behavior characterization and properties calculation ... MMP Measurements of Peavey #B1 Oil (Bemis-Shutts field) Temp: 108 F ... – PowerPoint PPT presentation

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Title: Carbon Dioxide Demonstration Project Supporting Research at KU


1
Carbon Dioxide Demonstration Project Supporting
Research at KU
  • Jyun-Syung Tsau
  • presented for
  • Tertiary Oil Recovery Project
  • Advisory Board Meeting
  • October 19-20, 2001

2
Supporting Research Activities
  • Simulation
  • Hall-Gurney field (LKC formation)
  • Bemis-Shutts field (Arbuckle formation)
  • Laboratory experiments
  • Slim-tube displacement
  • Residual oil measurement

3
Simulation
  • Reservoir simulator
  • VIP black oil simulator
  • Primary production, waterflooding
  • VIP compositional simulator
  • CO2 flooding

4
Compositional Simulator
  • Equation of state (EOS) for CO2-oil phase
    behavior characterization and properties
    calculation
  • Peng-Robinson 3-parameter EOS model

5
Typical Data Preparation for Compositional
Simulation
  • C7 characterization (sub-grouping heavy end)
  • Pseudoization (grouping)
  • Phase behavior calculation (swelling test)
  • Slim-tube displacement

6
Laboratory Displacement Data to Fine Tune
Reservoir Simulator
  • Slim-tube displacement experiment
  • Ideal porous media
  • Oil recovery attributed to phase behavior
  • MMP (minimum miscibility pressure) indicates the
    pressure required to develop multiple-contact
    miscibility
  • Fine tune EOS parameters in reservoir simulator

7
Schematic of Slim-tube Experiment Apparatus
8
Oil Recovery Performance in Slim-tube
Experiment(Letsch 7 oil)
Temp 105 F
9
MMP Measurements of Letsch 7 Oil
10
Oil Recovery Performance Match
11
Determination of Residual Oil Saturation to
Carbon Dioxide
  • Why it is important?
  • Miscibility developed by multiple contact results
    in variable amount of oil left behind in
    CO2-swept zone
  • Uncertainty in projection of oil recovery by the
    simulator

12
Critical Issues to the Measurements
  • Measurement needs to account for
  • Well defined development of miscibility
  • Representative fluid and rock properties

13
Schematic of Residual Oil Saturation Measurement
Apparatus
14
Characteristics of Slim-tube and Core Sample
15
Future Tasks
  • Investigate the effect of displacement rate, core
    length and structure on residual oil saturation
    determination
  • Investigate the effect of water saturation on the
    residual oil saturation to CO2

16
Evaluation of Arbuckle Crude Oil for Oil Recovery
by CO2 Displacement
  • Conduct experiment to measure MMP of crude oil
    obtained from Arbuckle formation
  • Perform simulation to match current field
    condition and test the reservoir response to
    pressurization process

17
MMP Measurements of Peavey B1 Oil (Bemis-Shutts
field)
Temp 108 F
18
Current Reservoir Condition
  • Average reservoir pressure is around 500 psia,
    which is not high enough for CO2 miscible
    displacement
  • Reservoir must be pressurized

19
Approaches
  • Construct a generic model to simulate the process
    of
  • Primary production
  • Pressurization
  • Model contains
  • 126 active production wells in a 2 by 2 square
    miles area (2560 acres)

20
Grid Cell System Used in the Model
21
Cross Section of the Reservoir Formation
  • 11 layers with permeability ranging between 0.2
    5 md in aquitard and 50 1500 md in production
    zones

22
Satisfactory Match
  • Simulation results were to match
  • Reservoir average pressure
  • Cumulative oil and water production
  • Current oil and water production rate

23
Observations
  • Reservoir is a layered reservoir with high
    permeability contrast between layers
  • Bottom water drive
  • Edge water drive does not provide enough energy
    to support the average reservoir pressure and
    production performance

24
Pressure Distribution at the End of Primary
Production (Beginning of Pressurization)
25
Simulation Tests to Pressurize a Project Area
  • 5 spot pattern (10 acres) with 6 confining
    injectors (within 120 acres)

26
Well Condition Parameters During the
Pressurization
  • Injector
  • 5-spot BHP 2000 psia, Qmax 3000 bbl/day
  • Confining area BHP 2000 psia, Qmax 3000
    bbl/day
  • Producer
  • 5-spot shut-in
  • Around confining area BHP 1100 psia, Qmax 300
    bbl/day
  • Other active producers BHP 300 psia, Qmax 300
    bbl/day

27
Pressure Distribution After 3-years
Pressurization
28
Summary of Pressurization Process
  • The magnitude of pressure increase within a
    pattern depends on the size of the pattern,
    confining area, and bottom hole pressure control
    of injectors and producers.
  • The ultimate pressures within the pattern varied
    from 1200 psia to 1500 psia.

29
Preliminary Results
  • Attainable reservoir pressure might slightly
    below the MMP as required for a miscible CO2
    displacement
  • Oil recovery remains relatively high (70 85)
    for a few hundred psi below MMP

30
Current Status
  • Oil and gas samples collected from the wellhead
    and separator were analyzed by Core-Lab
  • High nitrogen content was found on some of the
    separator samples through the quality check,
    which suggests the needs to measure MMP and oil
    recovery using a live oil sample
  • Detailed PVT test and swelling test would be
    conducted by Core-Lab, and data would be used for
    compositional simulation
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