Full Length ArticleThe influence of CO2 saturation time on the coal gas flow: Fractured bituminous coal
Introduction
Coalbed methane (CBM) is considered as a more clean-burning fuel, compared with traditional natural fuel counterparts such as coal and oil [1], [2], [3]. For example, the amount of carbon dioxide produced from a gas power plant is generally less than half (40–50 percent) of the carbon dioxide emitted from a coal power plant when generating the same amount of electricity [4]. Methane is originated during coalification process and can be basically found anywhere there is coal deposit [3]. The majority of CBM are strapped within microstructures through physical adsorption [2], therefore, unlike conventional natural gas reservoir, where the gas can flow towards the production wells to the surface without additional stimulation, coal seam water which is known as formation water needs to be pumped out to reduce the reservoir pressure before methane can be liberated from the coal seam. However, since coal seams are generally less permeable, methane recovered using this primary pressure depletion method is generally less than 50 percent [5]. Therefore, in order to achieve an economical methane harvest, additional stimulating method is required to be employed to increase the methane recovery rate.
To date, hydraulic fracking and enhanced coalbed methane (ECBM) recovery techniques are two options that can be adopted to increase the methane recovery rate, while the former is the most widely used technique to enhance the gas flow rate. However, despite the great effectiveness of increasing the methane recovery, controversies over environmental impacts of hydraulic fracking have been in discussion for years [6], [7], [8]. Enhance coalbed methane recovery technique is performed by injecting CO2, N2 or gas mixture into the target coal seam to replace the methane. Of the various ECBM methods, CO2-ECBM technique has an extra reward of immobilizing significant amount of CO2 into coal seam with the mechanism of residual trapping [9], which contributes to CO2 mitigation. During CO2-ECBM process, the more reactive CO2 acts as a displacement medium to admit the CH4 in-place to be desorbed from coal matrix, flow through seam fractures and eventually recovered via the production well with the CO2 to be sequestrated in the coal seam at the same time. Overall, a successful implementation of CO2-ECBM would harvest methane in an economical and environmental-friendly manner.
However, significant reduction of CO2 injectivity has been found both in lab-scale experiments [10], [11], [12], [13], [14], [15], [16], [17] and field scale projects [18], [19], [20], [21]. This permeability reduction is associated with coal matrix swelling during the adsorption of CO2 into coal matrix. As depicted in Fig. 1(a), coal possesses a unique porosity structure which can be viewed as a “dual porosity” system. This dual porosity system consists of a matrix porosity (micropores) and a cleat porosity (cleats or fractures), the latter accounts for most of the flow characteristics and therefore, controls the flow behaviours of the gases during ECBM process [22]. Coal originally has a strained, glassy, cross-linked macromolecular polymer-like structure which can be altered upon the adsorption of CO2 who plays as a plasticizer when interacting with the coal mass [23]. The structure of plasticized coal mass would be rearranged and large strain is therefore induced between the adsorbed CO2 gas layer and the surface of pore wall which is commonly known as coal matrix swelling [12]. The swelled coal structure would significantly narrow down the paths through which gas transportation primary occurs (see Fig. 1 (b)), resulting in a reduced coal seam permeability.
To date, a number of studies have been carried out to provide insights into coal mass hydro-mechanical properties alterations upon CO2 adsorption subjected to various experimental conditions. Table 1 summarises key findings by past authors on coal mass permeability alterations under different test conditions, those condition variables can be classified as coal seam properties, such as coal rank, coal seam buried depth, seam temperature, moisture content, and the properties of injecting gas, such as injection pressure, temperature and gas phase. Besides, the interaction time between coal mass and injecting gas also significantly affect the swelling process and degree.
Based on the information provided by Table 1, high rank coals tend to have much higher swelling effect upon the adsorption of CO2 compared with low rank coals [13], [15], [24], probably due to the maturely developed cleats system created by a much longer coalification process, which provides more places for housing CO2 molecule, resulting in a greater permeability reduction than low rank coals. Supercritical CO2 causes much higher permeability reduction than gaseous CO2 because of its more chemical reactive adsorption potential to coal [12], [15]. CO2 exists in its supercritical phase beyond the critical point (31.8 °C and 7.38 MPa), and in deep underground, where the temperature and pressure are generally higher than this critical point, permeability reduction due to supercritical CO2 adsorption would pose great challenges for CO2 injection during ECBM process since the favourable sites for implementation of CO2-ECBM are generally in deep buried coal seams [2]. Coal mass swelling degree with CO2 adsorption increases with time, and this process is one of the most vital aspects that keeps CO2 from successfully entering and sequestrating in coal seams, as reported by many in situ CO2-ECBM schemes [18], [19], [20], [21], for example, around 43% reduction of CO2 injectivity (from 4.3 t per day to 1.7 t per day) is observed in the Ishikari coal basin of Japan after 22 days of CO2 injection. This suggests the importance of the related studies on time-dependent permeability changes subjected to CO2 flooding. However, studies to date with regards to the effect of interaction time between coal and CO2 on flow behaviour alterations in coal are insufficient, especially for long term CO2 flooding. Perera et al. [12] observed a reduction trend of permeability with time using a naturally fractured black coal and this reduction ended within 3 days; similar results were also reported by Siriwardena et al. [29], a negative relation between swelling rate and time was recorded and swelling process was concluded within 3–4 days on an artificially-made-fractured anthracite. However, according to Ranathunga et al. [10], the amount of CO2 being adsorbed into coal increased over time even after 10 days flooding which indicates that permeability variation caused by CO2 adsorption did not end. As suggested by the model developed by Pan and Connell [30], though coal swelling ratio could reach a plateau and then decrease at very high gas pressures, coal swelling degree increases with the increasing amount of CO2 being adsorbed into coal mass. Besides, Structural re-arrangement of coal mass due to physical and chemical reactions between CO2 and coal mass could take place over time which may in turn cause alterations in the hydro-mechanical property of coal [31], [32].
Therefore, the main purpose of this study is to identify the influence of both subcritical and supercritical CO2 flooding time on permeability variations of naturally fractured low volatile bituminous coal under tri-axial conditions. Low volatile bituminous coal (high rank) was adopted as the favourable sites for carrying out CO2-ECBM pilots are in deep buried coal seam where high rank coals generally exist.
Section snippets
Sample preparation
Coal specimens used in this study are low volatile bituminous coals with natural fractures paralleled to the gas injection direction as shown in Fig. 2. Moisture content of the specimen is around 2.6%, and density of the coal specimen is 2.1 g/cm3. Coal specimens are prepared in the Deep Earth Energy Research Laboratory (DEERL) of Monash University. Specimens are cut and end trimmed into the standard size of 38 mm in diameter and 76 mm in length using the cutting and grinding machines available
Coal permeability variation upon sub-critical CO2 adsorption
N2 and CO2 permeability variations under corresponding injection pressure after each sub-critical CO2 flooding are displayed in Fig. 4. According to Fig. 4(a), N2 permeability increases with the increasing injection pressure for all the curves. For example, an increment of 23.53% was recorded for the initial N2 permeability when N2 injection pressure increases from 3 MPa to 5 MPa. Since N2 is generally considered as an inert gas, coal structure alteration induced by gas adsorption is
Conclusion
N2 and CO2 flow behaviours in the naturally fractured bituminous coal specimens were measured, and an attempt was made to evaluate the effect of sub- and super-critical CO2 flooding and its various action times on the permeability alteration of N2 and CO2 under three different confinements. The following conclusions can be drawn:
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N2 permeability increases with injection pressure regardless of buried depth due to the reduction of effective stress through enhanced pore pressure; while under low
Acknowledgements
Xiaogang Zhang would like to acknowledge the financial support from the China Scholarship Council and the Faculty of Engineering, Monash University.
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