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Hydrate Formation and Gas Production from Hydrates by CO 2 Injection - - PowerPoint PPT Presentation

U N I V E R S I T Y O F B E R G E N Institute of Physics and Technology Hydrate Formation and Gas Production from Hydrates by CO 2 Injection By Lars Petter ren Hauge uib.no Institute of Physics and Technology Natural gas hydrate


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U N I V E R S I T Y O F B E R G E N

Hydrate Formation and Gas Production from Hydrates by CO2 Injection

By Lars Petter Øren Hauge

Institute of Physics and Technology

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Natural gas hydrate

  • Crystalized structure consisting of water and a guest

molecule (e.g. methane) – resembles ice

  • High pressure (>30 bar) and low temperature (<10 °C)
  • Permafrost regions and off-shore

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Ota et al. (2005)

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Estimates of Total Gas Hydrate Amount

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Proven Crude Oil 2010 estimate by EIA (1358 BBOe) Most confident estimate by Claudia and Sandler 2005

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Hydrate

Reservoir strategies

  • Production scenarios
  • Pressure reduction
  • Temperature increase
  • Chemical additive
  • Exchange with CO2

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Hydrate

Injection of CO2 to produce methane

Pros Cons

  • Integrity of hydrate

structure remains intact

  • Sequestration of CO2
  • No temperature increase
  • Increased stability
  • Requires permeability
  • Risk of hydrate formation

from free water

  • Relatively slow rate of

exchange

  • Investment cost

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Experimental set up

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Gas supply High pressure pumps ISCO pump Confinement buffer Bypass valve Pressure transducer Thermocouple Sandstone core Safety pressure valve 1/8’’ tubing

MFM GC

Pressure regulator Back pressure valve Flow control valve Refrigerator bath Cooling jacket/bath Circulating antifreeze

Model made by Christian Hågenvik

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Experimental conditions

  • Porous media

– Bentheim sandstone – High permeable (1.1 D) – 20-25% porosity – Homogeneous (99% quartz)

  • Brine saturation 0.4 – 0.7
  • Brine salinity 0.1 – 3.5 wt% NaCl
  • Pressurized with CH4 to 83 barg/1200 psi
  • Temperature reduced from ~23 °C to 4 °C

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EXPERIMENTAL RESULTS

Methane Hydrate formation

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Same initial conditions

(system not dissasembled, only reformed)

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Hydrate formation

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Water saturation based on mass balance and resistivity

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Post Hydrate formation

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Limiting factor: lack

  • f water

Limiting factor: Mass transport – water trapping

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Post Hydrate formation

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Higher hydrate saturation for Swi ≈ 0.6 Limiting factor: Mass transport – water trapping Limiting factor: lack

  • f water
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EXPERIMENTAL RESULTS

CO2 induced methane production

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Experimental procedure

  • A back pressure valve maintains constant production

pressure of approximately 85 barg.

  • CO2, or a CO2/N2 mix, is injected at a constant flow rate
  • f 1.2 ml/h for all experiments.
  • Injection pressure, production pressure, gas fraction and

mass produced is monitored and later used to calculate differential pressure and fluids produced.

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Fraction of Methane during Production

Measured by GC

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Production during CO2 injection

Resistivity, gas produced and differential pressure

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Pressure build up

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Remediation of plugged core by use of N2

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N2 pressure buildup Inital CO2 injection Second CO2 injection

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CO-injection of CO2 and N2 (25/75 mol% resp.)

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Co-injection of CO2 and N2 N2 pressure buildup Injection of pure CO2

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CO-injection of CO2 and N2 (25/75 mol% resp.)

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Pure CO2 injection starts Injected N2 fraction Injected CO2 fraction

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Methane recovery

Free gas in porous media included

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