Flow Experiments of CO2 in Complex Pore Structures: History
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To prevent CO2 leakage and ensure the safety of long-term CO2 storage, it is essential to investigate the flow mechanism of CO2 in complex pore structures at the pore scale. 

  • CO2 storage
  • pore scale
  • complex pore structures
  • micro-flow

1. Introduction

Due to the increasing greenhouse effect as well as acute global climate and environmental problems, countries worldwide have reached a consensus to actively respond to climate change and reduce greenhouse gas emissions [1][2]. Since industrialization has continued since the industrial revolution, the use of fossil fuels has increased, and large amounts of CO2 gas have been directly discharged into the air, which is one of the main reasons for the intensification of the greenhouse effect [3]. CO2 emissions have led to a series of environmental problems, such as drought, glacier melt, and sea level rise, which have caused incalculable harm to the environment on which human beings depend [4]. At present, many technologies are available to control CO2 emissions, such as improving the efficiency of fossil energy combustion, the efficient development and utilization of green and clean energy, and carbon capture and storage (CCS) [5]. CCS refers to the use of separation and purification technology to collect a large amount of CO2 from industrial waste gas and inject it into appropriate underground reservoirs for permanent storage [6], which is recognized as one of the effective methods to manage CO2 [7]. At present, the membranes used for the selective transport of CO2 in the mixture of gases based on hollow alumina fiber-supported silica have been developed [8]. The application of this advanced technology greatly improves the efficiency of CO2 capture. The main geological layers used for storage include abandoned mines, unrecoverable coal seams, depleted oil and gas fields, deep saline aquifers, and the ocean [9]. The storage depth is generally below 800 m. CO2 geological storage is the most important part of CCS, and the storage capacity and safety of geological storage bodies determine the effectiveness of CO2 emission control [10]. Compared to other gases, CO2 is affected by temperature and pressure in the reservoir, and will produce phase transitions (gaseous, liquid, and supercritical). The microscopic flow of different phase states of CO2 in porous media is different. In addition, when CO2 flows in a reservoir, it can undergo physical and chemical reactions with reservoir water and matrix, causing damage to the reservoir. Meanwhile, the complexity, heterogeneity, and wettability [11] of the pores directly affect the flow behavior of CO2 in reservoirs. Therefore, investigating the CO2 flow law and revealing the CO2 microscopic flow mechanism are key for evaluating the storage capacity and safety of geological storage bodies.
Numerous studies have been conducted on the flow of CO2 in geological storage bodies. Lassen et al. [12] injected gaseous CO2 into heterogeneous porous media at different rates, and the flow of CO2 was monitored by sensors. The results showed that large-scale heterogeneity controlled the overall migration of gaseous CO2 in porous media, whereas a smaller scale was important for gas saturation. The higher the injection rate, the larger the transverse diffusion of the gas phase. Zhang et al. [13] proposed that Darcy’s law could be used to describe a two-phase fluid flow in porous media at the macroscopic scale. Saleem et al. [14] compared and verified the constructed two-phase flow model using field observation data, such as the CO2 eruption time, changes in the sediment pH, gas leakage rate, flow process, fluid interaction, and CO2 dissolution in the CO2 plume. The results showed that the CO2 plume was formed and developed at a stable rate during the flow process, and the dissolution rate increased with an increase in the injection rate. These studies elucidated the flow of CO2 from a macroscopic perspective. However, the flow behavior of CO2 in a storage body is easily affected by its complex pore structures. In macroscale research, the complex pore structures of the storage body have not been accurately characterized. The research results were also based on macroscale flow and often ignored the effect of the pore structure complexity. Therefore, an accurate description of the microscopic flow of CO2 is crucial for determining storage capacity and long-term safety [15].

2. Traditional Characterization of Pore Structures during CO2 Microscopic Flow

Mercury intrusion porosimetry (MIP) [16], scanning electron microscopy (SEM) [17], and gas adsorption [18] have been used to characterize the pore structures of the storage body and further explore the flow of CO2. Du et al. [19] used high-pressure mercury intrusion and permeation experiments to investigate the effect of CO2 injected into coal. The results showed that the reaction between CO2–water and coal led to an increase in the pore space and greatly increased the permeability, which increased the permeability area of CO2 and improved the CO2 storage capacity. Using SEM, Khather et al. [20] observed that a decrease in the pH during CO2 injection caused the dissolution and migration of minerals, which resulted in an increase in the rock permeability and flow capacity of CO2. Pearce et al. [21] studied the physical properties of the reservoir after CO2 injection using SEM and found that the movement of fine particles could result in opening or blocking the pores during CO2 injection, increasing or decreasing the permeability and affecting the CO2 injection capacity. Brattekas and Haugen [22] used high-resolution micro-positron emission tomography (micro-PET) and radiotracers to achieve CO2 tracing during the flow and capillary capture. The results showed that CO2 mainly flowed into the outer part of the core with a high permeability.
However, these techniques had numerous limitations for accurately characterizing the pore structure complexity in rocks. For example, MIP only obtained the total porosity of the sample and did not characterize the complexity of the pore distribution within the sample. SEM was an effective technique for generating 2D images of the microstructures. However, it did not provide 3D images, which were important for evaluating the pore structure complexity [5]. The measurement results obtained using gaseous adsorption methods were often constrained by the limited pore-scale range, and accurately characterizing the complexity of pore structures became challenging due to the size and interactions of the gas molecules [23]. More importantly, the traditional characterization methods did not visualize and quantitatively describe the microscopic flow of CO2. In addition, Tang et al. [24] conducted a comprehensive comparison of the rock pore structure characterization techniques, including experimental analyses, image analyses, and digital core techniques, and emphasized the importance of digital core techniques for solving complex pore structure characterization. Therefore, to accurately reconstruct the 3D complex pore structures and visually and quantitatively study the microscopic flow mechanism of CO2 in the geological storage body, it was necessary to use advanced techniques, such as CT scanning and NMR, to conduct an in-depth analysis using multidisciplinary intersection research ideas.
It is worth noting that with the continuous improvement of artificial intelligence (AI), some research applied it in the field for studying the microscopic flow of CO2 and achieved some remarkable results. A hybrid artificial intelligence model integrating a back propagation neural network (BPNN), genetic algorithm (GA), and adaptive boosting algorithm (AdaBoost) was proposed by Yan et al. [25], which was used to evaluate the change in the coal strength caused by the interaction between CO2 and coal in the flow process. Zhang et al. [26] proposed four advanced machine learning schemes, including RBFNN-MVO, RBFNN-GWO, RBFNN-PSO, and MLPLM, to evaluate the contact angle of various shale systems. Overall, AI plays a key role in predicting the parameters of complex pore structures as well as evaluating safety. In addition, the method of using AI to predict fluid flow is a hot topic for future research.

3. Effects of the Porosity and Permeability Characteristics on the Microscopic Flow Mechanism of CO2

The influence of the key parameters, including the porosity and permeability, on CO2 flow in geological storage bodies is very important. By simulating 2D fluid flow experiments, Kitamura et al. [27] found that the flow behavior of CO2 was strongly influenced by the small-scale heterogeneity of the pore structures. However, the simulation results had some errors since the model was 2D and could not fully describe the pore structure complexity. To investigate the effect of the reservoir laminar structures on the flow behavior of CO2, Krishnamuthy et al. [28] used the CT scanning technique to observe the flow path of CO2 by measuring the CO2 saturation variation in the rock. The results showed that CO2 preferentially flowed through the region with a larger porosity and passed unevenly along the axial direction. However, seepage under in situ conditions was not considered. Thus, the pore distribution in reservoir cores under in situ conditions could not be obtained. To accurately study the CO2 microcosmic flow, Wang et al. [29] injected liquid CO2 into a brine-saturated core. Multiscale CT scanning of sandstone was conducted and the distribution of the porosity at different locations in the core under in situ flow conditions was obtained. The phenomenon of CO2 preferentially passing through the locations with a higher porosity was observed from the images. Al-Bayati et al. [30] conducted a displacement experiment on the stratified core samples using the CT scanning technique. 
A clay interlayer, one of the typical representatives of a low-permeability layer, had an important influence on the CO2 flow. Using CT scanning, Xu et al. [31] studied the flow characteristics of CO2 in a special sandstone containing multiple thin clay interlayers. The experiment demonstrated that the flow channel of CO2 was mainly established in the sandstone, and the clay interlayer hindered the CO2 flow. However, the description of how the CO2 flow was hindered by the clay interlayer was too vague. Therefore, Xu et al. [32] further monitored the flow process of CO2 in the interior of the clay interlayer sample. When the injection direction was parallel to that of the clay interlayer, the clay interlayer separated the CO2 flow. When the injection direction was perpendicular to that of the clay interlayer, the clay interlayer hindered the forward CO2 flow.

4. Two-Phase Flow Law in CO2 Microscopic Flow

When CO2 was injected into the deep brine layer, it entered the reservoir pore structures to displace the original fluid from the pore space, and the flow process was an immiscible two-phase flow [33]. However, it was difficult to observe the space–time variation of the two-phase interface between the immiscible two-phase fluids in the porous media. Therefore, the immiscible two-phase flow needed to be understood from a pore-scale perspective, which was very important and extremely complex [34].
Using the CT scanning technique, Kogure et al. [35] injected CO2 into the Berea sandstone at different times in opposite directions, and the flow behavior of CO2 in the Berea sandstone was observed. The images showed several narrow pore throats that allowed for the CO2 flow. Despite injections from opposite directions, the distribution of CO2 was essentially the same in the final stage of injection. Liu et al. [36] injected CO2 into a glass bead bed in both the upward and downward directions, and a displacement-saturated water experiment was conducted to investigate the distribution of CO2 in the core. The displacement effect of CO2 injected downward was substantially better than that of CO2 injected upwards. This was attributed to the “gas channeling” phenomenon when CO2 was injected upward, but the cause of the “gas channeling” phenomenon was not discussed in depth. Lv et al. [37] combined the CT scanning technique and a micromodel to study the flow process of CO2–brine in the pore structures at different injection rates under static and transient conditions. The results showed that a higher injection rate caused a higher displacement efficiency but a lower sweep efficiency. Further, using the NMR technique, Teng et al. [38] found that the different viscosities and densities of CO2 and water caused the “gas channeling” phenomenon of CO2, which led to the premature breakthrough of CO2 and reduced the displacement efficiency. In addition, Zhang et al. [13] obtained the local porosity and saturation of the Berea sandstone. The results showed that the forward movement of CO2 on the capillary pressure was the main reason for the formation of the pathway of the CO2 flow. CO2 preferentially passed through the large-sized pores, and the seepage zone gradually expanded whereas the CO2 saturation increased.
The Influence of pore geometry on the microscopic flow mechanism of CO2 was not ignored. Zhang et al. [39] used CT scanning to scan the displacement process of CO2 and found that CO2 was unevenly distributed in the sandstone samples. A larger flow patch was formed during the flow process. Herring et al. [40] adopted the Bentheimer sandstone core and used the CT scanning technique to observe the displacement process of CO2 at the pore scale. The images showed that CO2 invaded the pore space in a capillary fingering regime. Liu et al. [41] visualized and quantitatively analyzed the dynamic diffusion process of CO2 in n-decane-saturated porous media. The results showed that the channels of the porous media hindered the diffusion of CO2. The local diffusion coefficient of CO2 gradually decreased with time along the diffusion path until it reached a steady state.

5. Microscopic Flow of CO2 in Different Phase States

In geological storage, appropriate CO2 phase states, including gaseous, liquid, and supercritical, should be selected according to the specific conditions and requirements of the storage body. CT scanning technology has been used to conduct extensive research on the microscopic flow of CO2 in different phase states. CO2 bubbles, a typical representative of the gaseous state, have a stable state in porous media with a high resistance factor (i.e., good plugging capacity), which plays an essential role in the safety of long-term storage of CO2 [42]. Xue et al. [43] found that microbubble CO2 injection minimized the content of free CO2 in the reservoir compared to that of conventional CO2 injection and also efficiently utilized the pore space of the reservoir, which was conducive to the long-term safety of large-scale CO2 storage. Patmonoaji et al. [44] and Zhai et al. [45] conducted displacement experiments in sandstone and found that the microbubble flow had a stronger sweeping efficiency than that of the conventional flow, which improved the displacement efficiency and storage capacity of CO2.
The experimental results proved that CO2 foam not only improved oil and gas recovery compared to conventional CO2, but also improved the pore space utilization and increased CO2 storage in the reservoir. Accordingly, Du et al. [46] further investigated the seepage characteristics of CO2 bubbles in porous media. However, the experimental object was self-made homogeneous porous media, whereas most of the actual reservoir was composed of heterogeneous rocks. Thus, the experimental results had some limitations. For this reason, McLendon et al. [47] injected CO2 with and without a surfactant into real Berea sandstone under high-pressure conditions to observe the in situ bubble generation. The results showed that CO2 tended to pass through the high-permeability reservoir without the addition of a surfactant but resulted in a decrease in the sweep efficiency of CO2. Du et al. [48] studied the dynamic bubble flow behavior in the entrance region of porous media and obtained dynamic three-phase saturation distributions along the sample core. The results showed that the CO2 bubble pushed most of the liquid phase into the latter part of the porous media, but the forepart was difficult to push, showing an obvious entrance effect.
The above studies investigated the microscopic flow of single-phase CO2. However, it was unusual that CO2 not only existed in the actual storage body, but two or multiphase may be present. Therefore, it was essential to further study the microscopic flow of CO2 under the condition of polyphase coexistence (including miscible, near-miscible, and immiscible phases). Alhosani et al. [49] conducted an in situ study on immiscible-phase CO2 displacement in oil-wet reservoirs. The images showed that in strongly oil-wet rocks, the largest pore space was occupied by water, the smallest pore space was occupied by oil, and the medium-sized pore space was occupied by CO2. CO2 was distributed in a connected layer under near-miscible-phase conditions and existed as separated “ganglia” in medium-sized pores under immiscible-phase conditions. Qin et al. [50] conducted a study on the wettability and spatial distribution of near-miscible-phase CO2 in oil-wet carbonate rocks under a high temperature and pressure. The results showed that at the initial stage of injection, CO2 had good connectivity with the oil phase and poor connectivity with the brine phase. With the continuous injection of CO2, the wettability reversal process was triggered, resulting in a decrease in the oil wettability and an improvement in the CO2 connectivity with brine. Hao et al. [51] conducted multi-phase and multiple injection experiments. It was found that under the immiscible-phase condition, the porous media showed remarkable gas coverage and flow stratification owing to gas buoyancy. The miscible-phase CO2 injection eliminated the effect of buoyancy, thus expanding the storage area and flow range of CO2.
The reliability of CO2 geologic storage depends on the flow mechanism of CO2 in reservoirs. Due to advanced imaging techniques such as CT scanning and NMR in experimental studies, it was beneficial to study the microscopic flow mechanism of CO2 in complex pore structures. However, few studies used CT scanning and NMR technology to conduct real-time visualization and quantification research on the microscopic flow process of CO2. In addition, microscopic flow studies of different phases of CO2 in complex pore structures were not sufficiently comprehensive, which will be the focus of future research.

This entry is adapted from the peer-reviewed paper 10.3390/su151712959

References

  1. Yu, S.; Zhang, Q.; Hao, J.L.; Ma, W.; Sun, Y.; Wang, X.; Song, Y. Development of an extended STIRPAT model to assess the driving factors of household carbon dioxide emissions in China. J. Environ. Manag. 2023, 325, 116502.
  2. Safaei-Farouji, M.; Vo Thanh, H.; Sheini Dashtgoli, D.; Yasin, Q.; Radwan, A.E.; Ashraf, U.; Lee, K.-K. Application of robust intelligent schemes for accurate modelling interfacial tension of CO2 brine systems: Implications for structural CO2 trapping. Fuel 2022, 319, 123821.
  3. Park, J.H.; Yang, J.; Kim, D. Review of recent technologies for transforming carbon dioxide to carbon materials. Chem. Eng. J. 2022, 427, 130980.
  4. Wu, S.; Wang, L.; Cai, Q.; Yan, X. Potential impact assessment for China’s dry and wet areas under global warming targets. Phys. Chem. Earth Parts A/B/C 2020, 116, 102838.
  5. Gan, M.; Zhang, L.; Miao, X.; Oladyshkin, S.; Cheng, X.; Wang, Y.; Shu, Y.; Su, X.; Li, X. Application of computed tomography (CT) in geologic CO2 utilization and storage research: A critical review. J. Nat. Gas Sci. Eng. 2020, 83, 103591.
  6. Yanzhong, W.; Nianmin, Z.; Xu, C.; Yingchang, C.; Guanghui, Y.; Gluyas, J.G.; Miruo, L. Geologic CO2 storage in arkosic sandstones with CaCl2-rich formation water. Chem. Geol. 2020, 558, 119867.
  7. Medina-Martos, E.; Gálvez-Martos, J.-L.; Almarza, J.; Lirio, C.; Iribarren, D.; Valente, A.; Dufour, J. Environmental and economic performance of carbon capture with sodium hydroxide. J. CO2 Util. 2022, 60, 101991.
  8. Araki, S.; Yamashita, R.; Li, K.; Yamamoto, H. Preparation and gas permeation properties of all-silica CHA zeolite hollow fiber membranes prepared on amorphous-silica hollow fibers. J. Membr. Sci. 2021, 634, 119338.
  9. Bui, M.; Adjiman, C.S.; Bardow, A.; Anthony, E.J.; Boston, A.; Brown, S.; Fennell, P.S.; Fuss, S.; Galindo, A.; Hackett, L.A.; et al. Carbon capture and storage (CCS): The way forward. Energy Environ. Sci. 2018, 11, 1062–1176.
  10. Cao, C.; Liu, H.; Hou, Z.; Mehmood, F.; Feng, W. A Review of CO2 Storage in View of Safety and Cost-Effectiveness. Energies 2020, 13, 600.
  11. Ragui, K.; Bennacer, R.; Chen, L. Pore-scale modeling on supercritical CO2 invasion in 3D micromodel with randomly arranged spherical cross-sections. Energy Rep. 2021, 7, 33–42.
  12. Lassen, R.N.; Plampin, M.R.; Sakaki, T.; Illangasekare, T.H.; Gudbjerg, J.; Sonnenborg, T.O.; Jensen, K.H. Effects of geologic heterogeneity on migration of gaseous CO2 using laboratory and modeling investigations. Int. J. Greenh. Gas Control 2015, 43, 213–224.
  13. Zhang, Y.; Kogure, T.; Nishizawa, O.; Xue, Z. Different flow behavior between 1-to-1 displacement and co-injection of CO2 and brine in Berea sandstone: Insights from laboratory experiments with X-ray CT imaging. Int. J. Greenh. Gas Control 2017, 66, 76–84.
  14. Saleem, U.; Dewar, M.; Chaudhary, T.N.; Sana, M.; Lichtschlag, A.; Alendal, G.; Chen, B. Numerical modelling of CO2 migration in heterogeneous sediments and leakage scenario for STEMM-CCS field experiments. Int. J. Greenh. Gas Control 2021, 109, 103339.
  15. Cheng, X.; Mei, K.; Li, Z.; Zhang, X.; Guo, X. Research on the Interface Structure during Unidirectional Corrosion for Oil-Well Cement in H2S Based on Computed Tomography Technology. Ind. Eng. Chem. Res. 2016, 55, 10889–10895.
  16. Zou, X.Y.; Li, X.Q.; Zhang, J.Z.; Li, H.; Guo, M.; Zhao, P. Characteristics of Pore Structure and Gas Content of the Lower Paleozoic Shale from the Upper Yangtze Plate, South China. Energies 2021, 14, 7603.
  17. Dai, X.; Wang, M.; Weia, C.; Zhang, J.; Wang, X.; Zou, M. Factors affecting shale microscopic pore structure variation during interaction with supercritical CO2. J. CO2 Util. 2020, 38, 194–211.
  18. Ozotta, O.; Liu, K.; Gentzis, T.; Carvajal-Ortiz, H.; Ostadhassan, M. Pore Structure Alteration of Organic-Rich Shale with Sc-CO2 Exposure: The Bakken Formation. Energy Fuels 2021, 35, 5074–5089.
  19. Du, Y.; Sang, S.; Pan, Z.; Wang, W.; Liu, S.; Fu, C.; Zhao, Y.; Zhang, J. Experimental study of supercritical CO2-H2O-coal interactions and the effect on coal permeability. Fuel 2019, 253, 369–382.
  20. Khather, M.; Saeedi, A.; Rezaee, R.; Noble, R.R.P. Experimental evaluation of carbonated brine-limestone interactions under reservoir conditions-emphasis on the effect of core scale heterogeneities. Int. J. Greenh. Gas Control 2018, 68, 128–145.
  21. Pearce, J.K.; Dawson, G.K.W.; Golab, A.; Knuefing, L.; Sommacal, S.; Rudolph, V.; Golding, S.D. A combined geochemical and μCT study on the CO2 reactivity of Surat Basin reservoir and cap-rock cores: Porosity changes, mineral dissolution and fines migration. Int. J. Greenh. Gas Control 2019, 80, 10–24.
  22. Brattekås, B.; Haugen, M. Explicit tracking of CO2-flow at the core scale using micro-Positron Emission Tomography (μPET). J. Nat. Gas Sci. Eng. 2020, 77, 103268.
  23. Clarkson, C.R.; Solano, N.; Bustin, R.M.; Bustin, A.M.M.; Chalmers, G.R.L.; He, L.; Melnichenko, Y.B.; Radliński, A.P.; Blach, T.P. Pore structure characterization of North American shale gas reservoirs using USANS/SANS, gas adsorption, and mercury intrusion. Fuel 2013, 103, 606–616.
  24. Tang, Y.; Hou, C.; He, Y.; Wang, Y.; Chen, Y.; Rui, Z. Review on Pore Structure Characterization and Microscopic Flow Mechanism of CO2. Flooding in Porous Media. Energy Technol. 2020, 9, 2000787.
  25. Yan, H.; Zhang, J.; Zhou, N.; Li, M. Application of hybrid artificial intelligence model to predict coal strength alteration during CO(2) geological sequestration in coal seams. Sci. Total Environ. 2020, 711, 135029.
  26. Zhang, H.; Thanh, H.V.; Rahimi, M.; Al-Mudhafar, W.J.; Tangparitkul, S.; Zhang, T.; Dai, Z.; Ashraf, U. Improving predictions of shale wettability using advanced machine learning techniques and nature-inspired methods: Implications for carbon capture utilization and storage. Sci. Total Environ. 2023, 877, 162944.
  27. Kitamura, K.; Kogure, T.; Nishizawa, O.; Xue, Z. Experimental and Numerical Study of Residual CO2 Trapping in Porous Sandstone. Energy Procedia 2013, 37, 4093–4098.
  28. Krishnamurthy, P.G.; Senthilnathan, S.; Yoon, H.; Thomassen, D.; Meckel, T.; DiCarlo, D. Comparison of Darcy’s law and invasion percolation simulations with buoyancy-driven CO2-brine multiphase flow in a heterogeneous sandstone core. J. Pet. Sci. Eng. 2017, 155, 54–62.
  29. Yan, W.; Crandall, D.; Bruner, K.; Ning, W.; Gill, M.; Xiaochun, L.; Bromhal, G. Core and Pore Scale Characterization of Liujiagou Outcrop Sandstone, Ordos basin, China for CO2 Aquifer Storage. Energy Procedia 2013, 37, 5055–5062.
  30. Al-Bayati, D.; Saeedi, A.; Myers, M.; White, C.; Xie, Q. Insights into immiscible supercritical CO2 EOR: An XCT scanner assisted flow behaviour in layered sandstone porous media. J. CO2 Util. 2019, 32, 187–195.
  31. Xu, L.; Li, Q.; Myers, M.; White, C.; Tan, Y. Experimental and numerical investigation of supercritical CO2 migration in sandstone with multiple clay interlayers. Int. J. Greenh. Gas Control 2021, 104, 103194.
  32. Xu, L.; Myers, M.; Li, Q.; White, C.; Zhang, X. Migration and storage characteristics of supercritical CO2 in anisotropic sandstones with clay interlayers based on X-CT experiments. J. Hydrol. 2020, 580, 124239.
  33. Xu, L.; Li, Q.; Myers, M.; Chen, Q.; Li, X. Application of nuclear magnetic resonance technology to carbon capture, utilization and storage: A review. J. Rock Mech. Geotech. Eng. 2019, 11, 892–908.
  34. Zhu, Q.; Zhou, Q.; Li, X. Numerical simulation of displacement characteristics of CO2 injected in pore-scale porous media. J. Rock Mech. Geotech. Eng. 2016, 8, 87–92.
  35. Kogure, T.; Nishizawa, O.; Chiyonobu, S.; Yazaki, Y.; Shibatani, S.; Xue, Z. Effect of Sub-core Scale Heterogeneity on Relative Permeability Curves of Porous Sandstone in a Water-supercritical CO2 System. Energy Procedia 2013, 37, 4491–4498.
  36. Liu, Y.; Wang, H.; Shen, Z.; Song, Y. Estimation of CO2 Storage Capacity in Porous Media by using X-ray Micro-CT. Energy Procedia 2013, 37, 5201–5208.
  37. Lv, P.; Liu, Y.; Yang, W. Investigation on CO2 permeation in water-saturated porous media with disordered pore sizes. Exp. Therm. Fluid Sci. 2020, 119, 110207.
  38. Teng, Y.; Liu, Y.; Lu, G.; Jiang, L.; Wang, D.; Song, Y. Experimental Evaluation of Injection Pressure and Flow Rate Effects on Geological CO2 Sequestration Using MRI. Energy Procedia 2017, 114, 4986–4993.
  39. Zhang, Y.; Park, H.; Nishizawa, O.; Kiyama, T.; Xue, Z. Fluid Distribution Effects on P-wave Velocity of CO2/brine Saturated Rocks: A Comparison Study and Implications for CO2 Storage Monitoring Using Seismic Method. Energy Procedia 2017, 114, 3786–3792.
  40. Herring, A.L.; Andersson, L.; Newell, D.L.; Carey, J.W.; Wildenschild, D. Pore-scale observations of supercritical CO2 drainage in Bentheimer sandstone by synchrotron x-ray imaging. Int. J. Greenh. Gas Control 2014, 25, 93–101.
  41. Liu, Y.; Teng, Y.; Lu, G.; Jiang, L.; Zhao, J.; Zhang, Y.; Song, Y. Experimental study on CO2 diffusion in bulk n-decane and n-decane saturated porous media using micro-CT. Fluid Phase Equilib. 2016, 417, 212–219.
  42. Khalil, M.; Liu, N.; Lee], R. Effect of particle hydrophobicity on CO2 foam generation and foam flow behavior in porous media. Fuel 2014, 126, 104–108.
  43. Xue, Z.; Nishio, S.; Hagiwara, N.; Matsuoka, T. Microbubble Carbon Dioxide Injection for Enhanced Dissolution in Geological Sequestration and Improved Oil Recovery. Energy Procedia 2014, 63, 7939–7946.
  44. Patmonoaji, A.; Zhang, Y.; Xue, Z.; Park, H.; Suekane, T. Experimental and numerical simulation of supercritical CO2 microbubble injection into a brine-saturated porous medium. Int. J. Greenh. Gas Control 2019, 91, 102830.
  45. Zhai, H.; Xue, Z.; Park, H.; Aizawa, Y.; Baba, Y.; Zhang, Y. Migration characteristics of supercritical CO2 microbubble flow in the Berea sandstone revealed by voxel-based X-ray computed tomography imaging analysis. J. Nat. Gas Sci. Eng. 2020, 77, 103233.
  46. Du, D.; Wang, D.; Jia, N.; Lyu, W.; Qin, J.; Wang, C.; Sun, S.; Li, Y. Experiments on CO2 foam seepage characteristics in porous media. Pet. Explor. Dev. 2016, 43, 499–505.
  47. McLendon, W.J.; Koronaios, P.; Enick, R.M.; Biesmans, G.; Salazar, L.; Miller, A.; Soong, Y.; McLendon, T.; Romanov, V.; Crandall, D. Assessment of CO2-soluble non-ionic surfactants for mobility reduction using mobility measurements and CT imaging. J. Pet. Sci. Eng. 2014, 119, 196–209.
  48. Du, D.; Li, Y.; Zhang, D.; Dong, X.; Wang, F.; Chao, K. Experimental study on the inlet behavior of CO2 foam three phase displacement processes in porous media. Exp. Therm. Fluid Sci. 2019, 103, 247–261.
  49. Alhosani, A.; Lin, Q.; Scanziani, A.; Andrews, E.; Zhang, K.; Bijeljic, B.; Blunt, M.J. Pore-scale characterization of carbon dioxide storage at immiscible and near-miscible conditions in altered-wettability reservoir rocks. Int. J. Greenh. Gas Control 2021, 105, 103232.
  50. Qin, Z.; Arshadi, M.; Piri, M. Near-miscible supercritical CO2 injection in oil-wet carbonate: A pore-scale experimental investigation of wettability state and three-phase flow behavior. Adv. Water Resour. 2021, 158, 104057.
  51. Hao, Y.; Li, Z.; Su, Y.; Kong, C.; Chen, H.; Meng, Y. Experimental investigation of CO2 storage and oil production of different CO2 injection methods at pore-scale and core-scale. Energy 2022, 254, 124349.
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