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Frontiers of Chemical Science and Engineering

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ISSN 2095-0187(Online)

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Front Chem Sci Eng    2011, Vol. 5 Issue (2) : 139-161    https://doi.org/10.1007/s11705-010-0527-4
REVIEW ARTICLE
A review on transport of coal seam gas and its impact on coalbed methane recovery
Geoff G.X. WANG1,3,4(), Xiaodong ZHANG1,2, Xiaorong WEI1, Xuehai FU3,4, Bo JIANG3,4, Yong QIN3,4
1. School of Chemical Engineering, the University of Queensland, Brisbane, Qld 4072, Australia; 2. School of Resources & Environment, Henan Polytechnic University, Jiaozuo 454000, China; 3. School of Resource and Geosciences, China University of Mining and Technology, Xuzhou 221008, China; 4. Key Laboratory of CBM Resources and Dynamic Accumulation Process, Ministry of Education of China, Xuzhou 221008, China
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Abstract

This paper presents a summary review on mass transport of coal seam gas (CSG) in coal associated with the coalbed methane (CBM) and CO2 geo-sequestration enhanced CBM (CO2-ECBM) recovery and current research advances in order to provide general knowledge and fundamental understanding of the CBM/ECBM processes for improved CBM recovery. It will discuss the major aspects of theory and technology for evaluation and development of CBM resources, including the gas storage and flow mechanism in CBM reservoirs in terms of their differences with conventional natural gas reservoirs, and their impact on CBM production behavior. The paper summarizes the evaluation procedure and methodologies used for CBM exploration and exploitation with some recommendations.

Keywords mass transport      coal seam gas (CSG)      coalbed methane (CBM)      coal      CBM recovery      carbon dioxide storage     
Corresponding Author(s): WANG Geoff G.X.,Email:gxwang@uq.edu.au   
Issue Date: 05 June 2011
 Cite this article:   
Geoff G.X. WANG,Xiaodong ZHANG,Xiaorong WEI, et al. A review on transport of coal seam gas and its impact on coalbed methane recovery[J]. Front Chem Sci Eng, 2011, 5(2): 139-161.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-010-0527-4
https://academic.hep.com.cn/fcse/EN/Y2011/V5/I2/139
characteristicNGCSG
generationgenerated in the source rock and then migrates into the reservoirs from external sources (source rock).generated in situ by microbial activity and/or thermogenic processes and trapped within the coal.
compositioncommonly composed of methane plus lesser amounts of higher molecular weight hydrocarbons including hydrocarbon liquids.mostly methane (up to 95% - 98%) and very few carbon dioxide and other components.
reservoir structurerandomly-spaced fracturesnetworking-spaced cleats
storage mechanismcompressed and trapped in the interstitial pore spaces (porosity) between sand (or other clastic) grains.adsorbed and trapped by molecular bonding (adsorption) on the internal surfaces of micropores within the coal.
transport mechanismpressure gradient (Darcy’s Law)concentration gradient (Fick’s Law) and pressure gradient (Darcy’s Law)
production performanceassociated with water production only in the latter field (Fig. 1(a)). As result, gas rate starts high then decline. Gas-Water-Ratio decreases with time.usually preceded by water production (Fig. 1(b)), so gas rate increases with time then declines. Initially the production is mainly water. Gas-Water-Ratio increases with time.
mechanical propertiesYoung modules 4 × 104 - 4.5 × 104 MPapore compressibility ~10-5 Mpa-1Young modules 1 × 103 - 3 × 103 MPapore compressibility ~10-3 MPa-1
Tab.1  Summary of differences between CSG and conventional natural gas (NG) productions
Fig.1  Gas and water productions during a) natural gas production and b) CBM production
Fig.2  Typical coal structure (a) coal sample with cleat marks and (b) physical representative []
Fig.3  Multi-scale gas transport in coalbed (after Law et al. with modification)
processparameterrole
desorptionLangmuir pressure, PL (MPa)Langmuir volume, VL (cm3/g)determination of gas content or adsorption/desorption capacity of CBM reservoir
diffusionsorption time, τ (day)diffusivity, D (cm2/s)micro-permeability, k (md)controlling microspore transport, i.e. migration of gas molecules in microspores of coal
darcy flowpermeability, k (md) dominating gas transport in cleats/features of coal
Tab.2  Transport properties of coal and their roles in CBM recovery
Fig.4  Coupling processes during gas transport in coalbed
Fig.5  A typical framework of diffusion models for CBM recovery []
assumptions and modeling methodsRuckenstein et al. [61]Clarkson , Bustin [10]Shi, Durucan [62]Cui et al. [65]Mazumder et al. [60]Siemons et al. (2003) [63]
sorption equilibrium
 adsorption occurring only in micropores
 linear isotherm
 nonlinear isotherm (Langmuir isotherm)
 extended Langmuir isotherm
sorption kinetics
 a step change in external concentration
 time-varying boundary pressure
 first-step diffusion (micropores)surface diffusion and Knudsen diffusionsurface diffusionsurface diffusion and Knudsen diffusionsurface diffusionsurface diffusion
 second-step diffusion (macropores)molecule diffusionmolecule/transition diffusion and/or Knudsen diffusionmolecule diffusionmolecule/transition diffusion and/or Knudsen diffusion
 pseudo-steady-state (Warren, Root)
 unsteady-state equation
 multicomponent gas diffusion(Fick law)
 constant diffusivity
 concentration-dependent diffusivity
 pressure-dependent diffusivity
assumption of pore structure
 the adsorbent particle contains uniform radius microporous microspheres with the space between microspheres making up the macroporositya little different
water effects on gas diffusivity
inversion of gas diffusivities
 two fitting parameters
 one parameter (micropore diffusivity)
Tab.3  Various bidisperse diffusion models for CBM recovery
Fig.6  Combined effects of mechanical deformation and sorption-induced swelling/shrinkage on Permeability change during CBM recovery (after Robertson with modification)
Fig.7  An advanced strain gauge method for measurement of sorption-induced strain in coal (after Massarotto [] with modification)
Fig.8  A typical optical method for measurement of sorption-induced strain in coal (After Day et al. [])
coalsorbed gassorption-induced strainpressure a)reference
typevalue /%
variousCH4volumetric0.2 - 1.6~15.2 MPaMoffat, Weale [73]
kentucky coalsCO2volumetric1.3120 psiReucroft, Patel [74]
unclearCH4longitudinal0.06800 psiGray [25]
CO2longitudinal1.0800 psi
unclearCH4volumetric0.61000 psiHarpalani, Schraufnagel [23]
bituminousCO2volumetric0.36-1.310.41 MPaHarpalani, Chen

Harpalani S, Chen G. Effect of gas production on porosity and permeability of coal. In: Symposium on Coalbed Methane, Townsville, Australia. 1992, 67-68

unclearCH4longitudinal0.11000 psiSeidle, Hutti [31]
CO2longitudinal0.8800 psi
high-volatile bituminousCH4longitudinal0.21000 psiLevine [30]
CO2longitudinal0.5750 psi
sub-bituminousCO2longitudinal0.00182/MPaSt. George, Barakat [36]
unclearCH4volumetric0.51000 psiZutshi, Harpalani

Zutshi A, Harpalani S. Matrix swelling with CO2 injection in CBM Reservoirs and its impact on permeability of coal. In: Proceedings of the 2004 International Coalbed Methane Symposium, Tuscaloosa, Alabama. 2004, Paper 0425

CO2volumetric1.1750 psi
unclearCH4volumetric0.491000 psiChikatamarla, Bustin [69]
CO2volumetric2.41800 psi
bituminoussub-bituminousCO2longitudinal0.2-0.3101.325kPaFry etc. [72]
volumetric0.3-5.0
bituminousCH4volumetric0.65~8.1MPaVan Bergen etc. [71]
CO20.37 - 0.92
Ar0.63
sub-bituminousCO2volumetric1.05 - 1.49~8.1MPaVan Bergen etc. [71]
Tab.4  Sorption induced strain data of some coals as reported in literature
Fig.9  Determination of gas content using direct method at a well test in Qinshui basin, China: a) Measurement of desorbed gas content; b) Graphic analysis for lost gas content; and c) Measurement of residual gas content
authorsmodelsnotes
Gray [25]σ-σ0=-ν1-ν(p-p0)+E3(1-ν)Δ?sΔpsΔpsk=1.013×10-3e-0.714σ (μm2)Δps: change in equivalent sorption pressureΔ?sΔps: strain caused by a unit change in equivalent sorption pressurematrix shrinkage proportional to reduction in equivalent sorption pressure
Harpalani, Zhao [93]k=Ap+B+Cp; A, B and C are constantspurely empirical
Sawyer et al. [77]?=?0[1+cp(p-p0)]-cm(1-?0)(ΔpΔC0)(C-C0)kk0=(??0)3based on pressure data for active (sorptive) gas; introduced into COMET model in 2002
Seidle, Huitt [31]??0=1+(1+2?0)?l(bp01+bp0-bp1+bp); kk0=(??0)3matrix shrinkage effect only
Palmer, Mansoori [75]?-?0=1M(p-p0)-(1-KM)?l(pp+p?-p0p0+p?)kk0=(??0)3 with fractions: M=E(1-ν)(1+ν)(1-2ν); K=E3(1-2ν)based on rock physical properties; Permeability can rebound at lower drawdown pressures if the matrix shrinkage is strong enough
Gilman, Beckie [92]k=k0exp?(3ν1-νp-p0Ef)exp?(3αE1-νΔSEf)α: volumetric swelling coefficient ; ΔS: change of the adsorbate mass?Ef: some analog of Young’s modulus for a fracturethe parameter Ef is not specified
Shi, Durucan [94]σ-σ0=-ν1-ν(p-p0)+E3(1-ν)j=1nαsj(Cμj-Cμj0)Cμj=VLjpyjbj1+pj=1nyjbj; kk0=(?c?c0)3=e-3cf(σ-σ0)integrated into Imperial model
Wang et al. [80]kj=kj0i=xz[ζi(1-?i+)n(1-δij)] (j=x,y,z)?i+=σi-σi0Ei-j=xz[(1-δij)νji(σj-σj0)Ej]+λ?s++αΔT (i=x,y,z)coal structure based; deformation and direction dependent; Not fully validated yet
Tab.5  Comparison of coal permeability models
Fig.10  Typical logging curves of a) strains and b) permeability resulted from TTSCP apparatus for CO flush tests in coal []
Fig.11  Pressure transient method for measurement of coal permeability (modified after Siriwardane et al. [])
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