Sequestration in Coal Seams: An Overview
Grant S. Bromhal
Carbon Sequestration Leadership Forum
National Energy Technology LaboratoryPittsburgh, PA
May 11, 2007
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Coalbeds are a major source of natural gas.*
• 3000 to 9000 Tm3
estimated global resource
• 8 to 17 Tm3 estimated U.S. resource
• Estimates of between 155 and 185 Billion tonnes of CO2 storage capacity in North American coals
*C.M. White, D.H. Smith, K.L. Jones, et al,”Sequestration of Carbon Dioxide in Coal with Enhanced Coalbed Methane Recovery--A Review,” Energy & Fuels 19, 659-724 (2005).
Data from Energy Information Administration. U.S. Crude Oil, Natural Gas, and Natural Gas Liquids Reserves 2003 Annual Report, Table 12.
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lbed
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hane
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oduc
tion
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Production from coal can be a complex process.
• Flow through coal is defined in large part by the cleat network.
• Methane sorbed on the coal is released by decreasing pressure.
• Water needs to be moved out of cleats before gas can flow.
• CO2 injection causes reverse process (adsorption instead of desorption.
SORPTION DIFFUSION ADVECTION
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Often, gas production is inhibited by initial water production.
• Relative permeability in the cleats affects flow of gas.
• Most of the water around the injection area should be removed before CO2 is injected.
Meek and Levine, 2006
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CO2 sequestration in coal will occur with ECBM.
• Five-spot pattern for thick coals (San Juan Basin)
• For thinner seams, horizontal wells may be used.
<915 m(<3000 ft)
Lateral #11
Well A
Well C
Well B
Lateral #6
Lateral #5
Lateral #7
Lateral #12 Lateral #10
Lateral #9
Lateral #8
AAPilot holes forLaterals #9 and #10
Pilot holes forLaterals #11 and #12
305 m(1000 ft)
<915 m(<3000 ft)
305 m(1000 ft)
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How much CO2 can be stored (and methane removed)?
• Sorption is typically considered to follow a Langmuir isotherm.
• The gas pressure in the coal seam determines how much is sorbed to the coal.
• CO2 is preferentially sorbed to coal, compared to methane.
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Original Coal
Coal shrinkage and swelling can have significant impact of cleat permeability.
• Based on the Palmer-Mansoori model
• Most important effect is on permeability
• Most important coal properties for shrinkage and swelling:− Porosity (φ)− Young’s modulus (E)− Poisson’s ratio (ν)
Coal matrix
Cleat space
Coal ShrinkageCoal Swelling
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Swelling may significantly reduce cleat permeability and therefore injectivity.
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Concluding Statements
• We have a couple of decades of experience in CBM production.
• CO2-ECBM is still in its infancy and much is being learned.
• A lot of capacity may be available.• Swelling could prove to be a big issue.
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We found optimum engineering designs for many different values of the coal properties.
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Injector Length (ft)
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bon
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xide
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d (M
MSC
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Inj pressure=300psiaInj pressure=400psiaInj pressure=500psiaInj pressure=600psiaInj pressure=700psia
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hane
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Inj pressure=300psiaInj pressure=400psiaInj pressure=500psiaInj pressure=600psiaInj pressure=700psia
Injector Length (ft)0 200 400 600 800 1000 1200
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hane
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duce
d (M
MSC
F)
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We found which physical parameters are most important for sequestration economics.
• Vertical wells.• DOE horizontal well project:
− Shorter injectors better for enhanced gas production, but not for sequestration.
− Natural gas price important for profitability, but for the cases studied, had little effect on optimal design.
− CO2 price/credit determines optimized design.
• Initiated discussions for possible addition to IECM.
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Young’s Modulus x (106) kPa
6 PoissonRatio
NP
V (M
$)
For the Technology Opportunity “modeling studies of swelling,” we predicted which petrophysical
parameters are economically important.*
• Young’s modulus generally more important than Poisson’s ratio.
• Preferred cleat porosity depends on Young’s modulus.
*Sequestration Technology Roadmap
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Our simulations and experiments are mutually supportive.
• CT imaging of coal cores: before, during, after injection
• Petrography
• Gas sorption and uptake rates, at lithostatic pressures
• Young’s modulus, etc.
• DEMONSTRATED THAT SORPTION ISOTHERMS ARE NEEDED AT LITHOSTATIC PRESSURES.
E x c e s s a d s o r p t i o n i s o t h e r m s f o r C a r b o n D i o x i d e o n a s r e c e i v e d B a i l e y M i n e C o a l
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mof
AR
Coa
l)
C o r e
P o w d e r T = 2 9 9 . 6 5 K
T = 3 0 3 K
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