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Article

Evaluation of the Potential for CO2 Storage and Saline Water Displacement in Huaiyin Sag, Subei Basin, East China

1
Center for Hydrogeology and Environmental Geology Survey, China Geological Survey, Tianjin 300304, China
2
Key Laboratory of Carbon Dioxide Geological Storage, China Geological Survey, Tianjin 300304, China
*
Authors to whom correspondence should be addressed.
Processes 2024, 12(3), 547; https://doi.org/10.3390/pr12030547
Submission received: 7 February 2024 / Revised: 3 March 2024 / Accepted: 8 March 2024 / Published: 11 March 2024

Abstract

:
CO2 geological storage combined with deep saline water recovery technology (CO2-EWR) is one of the most effective ways to reduce carbon emissions. Due to the complex structural features, it is difficult to use CO2-EWR technology in Huaiyin Sag, Subei basin, East China. In this study, the multi-source information superposition evaluation technology of GIS was utilized for the selection of CO2 storage sites and water displacement potential target areas in this area, which mainly focused on the sandstone reservoirs of Cretaceous Pukou Formation. Based on the results, a three-dimensional injection–extraction model was established. Various scenarios with different production/injection well ratios (PIR) were simulated. Research has shown that the suitability of the surrounding site of Huaiyin Power Plant can be divided into two levels: relatively suitable and generally suitable; the area in the generally suitable level accounts for more than 80%. At a PIR of 1, CO2 is distributed asymmetrically, whereas at PIRs of 2 or 4, CO2 is distributed symmetrically. When the number of production wells is constant, a higher injection rate results in a faster expansion rate of the CO2 plume. This means that the time taken for the CO2 plume to reach the production wells is shorter. Reservoir pressure increases rapidly after more than 60 years of CO2 injection at lower PIR values, while at higher PIRs, reservoir pressure eventually stabilizes. Higher PIR values correspond to higher gas saturation, indicating a greater capacity for CO2 sequestration with more producing wells. When PIR = 4, the total CO2 injection increased by 55.73% compared to PIR = 1. However, the extraction of saline decreases with an increase in the number of producing wells, resulting in a decrease in replacement efficiency. This study provides a theoretical basis and technical support for the implementation of large-scale CO2-EWR engineering and technology demonstration in this region.

1. Introduction

In response to global climate change, governments and institutions of all countries have successively put forward the targets of “carbon peaking” and “carbon neutrality”. CO2 emission reduction has become a hot issue in recent years [1,2,3,4,5,6,7,8]. CO2 storage in deep salt-water formation is one of the most effective ways for carbon emissions reduction [9,10,11,12,13,14,15,16,17,18]. A deep salt-water layer is widely distributed in China, which has a potential of up to 1.44 × 1011 t for CO2 storage in the buried depth range of 1–3 km [9]. However, large-scale CO2 storage in deep salt-water layers could cause rapid accumulation of reservoir pressure, which may promote reactivation of sealed fractures or create new fracture in the caprock seal. So, the caprock integrity may be damaged in the long term as a result of the CO2 sequestration in deep saline aquifers [19,20]. In terms of this issue, CO2 geological storage combined with deep saline water recovery technology (CO2-EWR) was proposed by Li and Bergmo [21,22,23]. CO2-EWR is the process in which CO2 is injected into deep saline or brine layers to displace high value-added liquid mineral resources (such as lithium salts, potassium salts, and bromine) or deep saline water resources, which can be comprehensively developed and utilized, while the injected CO2 is stored in the long term. This technology could not only meet the requirements of safe CO2 storage, but also provide a large amount of brine resources [21,23].
Scholars have conducted extensive research on CO2-EWR technology [13,14,15,16,17,18]. The effects of reservoir porosity, permeability, and total dissolved solids in salt water on CO2 storage capacity and salt water extraction were studied by using a homogeneous model in the Junggar Basin, China [24]. Li et al. evaluated the comprehensive utilization potential of CO2 flooding and storage in the deep salt water layer of the Shiqianfeng Formation in the Ordos Basin through experiments and numerical simulations [25]. Much research has shown that reservoir physical parameters, salinity, and boundary conditions all affect pressure changes and CO2 storage efficiency during CO2 injection and saline water extraction, and the formation pressure is an important factor limiting CO2 storage capacity [26,27,28,29,30]. In addition, the injection and output parameters (i.e., maximum injection of CO2 and the maximum production of salt water) have shown strong differences as the CO2-EWR injection production mode changes [31,32,33].
As a national thermal power plant, Huaneng Huaiyin Power Plant plays an important role in power supply in northern Jiangsu Province, and is under great pressure to reduce carbon emissions. It is of great practical significance to use CO2-EWR technology in this region. The good matching of sources and sinks, combined with a larger area of the saline water storage site, provide the feasibility of a large-scale geological storage project for CO2. However, the typical characteristics of geological background (i.e., small, fragmented, poor, and scattered) increase the difficulty of implementing the project in the Subei Basin [34,35]. Additionally, the development of the Huaiyin-Xiangshui Fault and the Tanlu Fault has increased the risk of geological hazards and limited the storage of large-scale CO2 saltwater layers in the Huaiyin Sag. The multi-source information superposition evaluation technology of GIS was utilized for the selection of CO2 storage sites and water displacement potential target areas in this area. Based on the site selection results, a geological model is constructed according to the actual geological conditions of the favorable area. As the study area is currently in the pre-study stage, numerical simulation has been employed to analyze the distribution characteristics of CO2 and the changes in reservoir pressure under different injection and extraction ratios. This will help to address any potential issues that may arise during the actual project.

2. Geological Setting

The Huaiyin Sag is a secondary structural unit of the Yanfu Depression in the Subei Basin, forming a dustpan-like structure. It is bounded by the Coastal Uplift to the northeast, the Huaiyin-Xiangshui fault to the west, the middle part of the Jianhu Uplift to the south and the Tangwa-dalaba high to the east (Figure 1). The structural pattern of the Subei Basin is controlled by the northeast and almost east–west faults. Generally, the study area is a low-amplitude anticline structure with many fault structures developed in this area, which are mainly polyphase, directional and inheritance normal faults that formed in the late Yanshan and Himalayan periods.
The Cretaceous Pukou Formation, which is the target formation of this study, has deposited an almost kilometer-thick saline series consisting of anhydrite, halite, and glauberite. The Pukou Formation was deposited in the pre-lake and semi-deep lake subfacies. Taking gypsum salt rock layers as the standard layer, and combined with sedimentary cycles characteristic, electrical characteristics, and well drilling data, the Pukou Formation can be divided into four sections (Kp4, Kp3, Kp2, Kp1) from top to bottom (Figure 2). The member 4 section of Pukou Formation (Kp4), which is mainly brown mudstone, could be a high-quality regional cap rock. The sandstone in the member 3 section of Pukou Formation (Kp3) is mainly composed of argillaceous rock debris feldspar quartz powder fine sandstone, with well to medium sorted and a high content of impurities, and the cementation type is mainly the poring contact type. The physical properties of the reservoir are highly variable, with porosity and permeability ranging from 0.4% to 8.3% (with an average of 5.38%) and 0.044–1.5 mD (with an average of 0.665 mD), respectively, indicating that the sandstone belongs to a low-porosity and low-permeability reservoir. The sandstone in the member 2 section of the Pukou Formation (Kp2) is mainly composed of fine–medium sandstone containing mud, ash, and cloudy feldspar debris with moderate sorting. The pores are mainly intergranular dissolution pores in this section, with porosity and permeability ranging from 0.6% to 15.55% (with an average of 6.82%) and 0.89–6.49 mD (with an average of 0.89 mD), respectively, indicating that the sandstone belongs to a medium- to low-porosity and low-permeability reservoir. The sandstone in section Kp1 of the Pukou Formation, known for its medium–low porosity and low permeability, is primarily composed of coarse to medium sandstone with gravel and feldspar debris. The reservoir and cap conditions in the study area are generally favorable.

3. Site Selection Evaluation

The assessment of CO2 saline water reservoir storage site selection is mainly based on the principles of maximum storage capacity, safety, minimum impact on resource development and utilization and economy. The evaluation is mainly conducted from three indicator layers and nine indicators, that is: geological suitability of the sink (reservoir conditions and storage potential, geological characteristics of top cap rock, seismicity, mutual feedback effect of energy development), surface suitability of the sink (geological hazard susceptibility, population density, terrain complexity) and economy (underground economy, CO2 pipeline transmission and land occupation cost). At present, there are many methods suitable for evaluating the suitability of CO2 geological storage, including empirical and mathematical methods (such as the analytic hierarchy process, probability analysis, and the feature–event–process (FEP) algorithm), as well as computer technology (such as multi-factor layer by layer stacking method in GIS environment). These evaluation methods are relatively mature and widely used [36,37,38,39,40,41,42]. Normally, the multi-source information superposition evaluation technology of GIS is utilized for the selection of CO2 saline water storage sites and water displacement potential target areas [43,44]. In this study, this method was also be used for the selection of CO2 saline water storage sites and water displacement potential target in the Huaiyin Sag.

3.1. Multi-Source Information Overlay Evaluation Technology

With the development of computer technology and remote sensing technology, the multi-source information superposition evaluation technology was proposed for the comprehensive processing of multi-source geoscience information (such as geographic information, geological information, and remote sensing information) [43,44]. It is based on the spatial two-dimensional plane determined by geographical coordinates to achieve the unity of geographic coordinates for the same region and different information, which is also known as spatial registration. The research work is completed by using geographic information software spatial analysis. The superposition of multiple sources of information is not a simple superposition of several types of information, but often leads to new information that cannot be provided by the original individual information.
The multi-source information overlay processing method is used to study the site selection of CO2 geological storage sites. Firstly, based on a systematic analysis of the influencing factors of CO2 geological storage, a thematic information map is prepared for each factor by using the basic function of GIS. Secondly, each thematic map generates an information storage layer which has been edited. Third, based on the single-factor analysis, registration and composite processing of major control factors are carried out to form a new information storage layer with composite overlays. Finally, a site selection suitability evaluation model is constructed to conduct site screening suitability evaluation in the research area.

3.2. Storage Site Selection

The Cretaceous Pukou Formation residual thickness is differentially distributed in the study area, two thickness centers were developed in Huaiyin Sag and Yancheng Sag, with a general thickness of 1500 m. In the middle of the study area, the Pukou Formation has experienced uplift and seriously denudation, which result in a thickness of approximately 500 m preserved in here. The Huaiyin-Xiangshui fault and the Tanlu fault were developed in the northwestern margin of the study area, and pose significant geological safety risks. Overall, the storage capacity in the areas of Huaiyin Power Plant and its surrounding is moderate to low, making it unsuitable for large-scale CO2 saline water storage. Therefore, it is necessary to optimize the storage location in the study area.
The feasibility evaluation of CO2 saline water storage is shown in Table 1. Through the data and information of regional geology, hydraulic and environmental geology, oil and gas geology, geophysical exploration and drilling data, as well as remote sensing interpretation, the reservoir cap rock combination, sedimentary facies changes, physical parameters and their spatial distribution and tectonics model were basically obtained. The characteristics of the evaluation area in terms of population density, topographical complexity and susceptibility to geological hazards were also taken into account, and the principles of “combining underground and surface, and combining technology and economy” were followed.
The hydrogeological characteristics, as an important parameter for storage site selection, are controlled by various factors such as natural geography, geological structure, lithofacies paleogeography and meteorological and hydrological conditions. The aquifer system in Huaiyin Sag mainly includes phreatic water in Quaternary loose sedimentary and pore phreatic water and interlayer water in Cretaceous clastic rock, among which the latter is the CO2-EWR technology reservoir cap rock area. The sediments of the Pukou Formation in this area exhibit a gradual evolution of salinity, from no salt at the bottom to more salt, less salt, and back to no salt at the top, vertically. Horizontally, the sediments show a pattern of increasing salinity from the subsidence center of the depression to the surrounding area, with a sequence of more salt, gypsum salt, gypsum mudstone, and sand mudstone. These observations suggest that the underground hydrogeological conditions in this area are favorable for the application of CO2-EWR technology.
The Pukou Formation in the study area lacks oil and gas resources, resulting in an abundance of groundwater in the sandstone reservoir. Additionally, the area has plentiful salt resources, primarily located in the middle section of the Pukou Formation. This section is mainly composed of clastic rock, sulfuric acid rock, and salt rock, forming a sedimentary sequence of normal sedimentary rocks and halites. During the salt formation period, the water solution undergoes repeated cycles of desalination, salinization, and desalination again. Additionally, the rhythm of salt-bearing strata changes frequently. This sedimentary background results in high mineralization of the groundwater in the sandstone aquifer, which enhances the industrial value of displacing saline water. As a result, the study area shows promising potential for saltwater mining.
The cap rock characteristics are important indicators of the geological safety for CO2 storage. The regional stratigraphic stability, lithology, thickness, burial depth, and other characteristics jointly determine the level of risk of CO2 leakage in geological storage under structurally stable conditions. When discussing the types of rock which suit to serve as cap rock, it is generally believed that evaporite has the best sealing ability, followed by argillaceous rock with medium sealing ability, and shale and tight limestone with the worst sealing ability. The thickness of cap rock also plays a crucial role in preventing the upward escape of oil and gas. A cap rock with a thickness greater than 100 m is considered good, while a thickness between 50 and 100 m is medium, and a thickness between 10 and 50 m is poor. It is believed that caprock has the best sealing ability when buried between 1000 m and 2700 m. This is due to the higher porosity and permeability of shallow caprock, and the increased brittleness of caprock, which leads to the formation of micro-cracks, at greater burial depths (i.e., more than 2700 m). The cap rock in the study area consists mainly of mudstone and salt rock. It is a single layer with a thickness ranging from 90 m to 130 m and burial depth in range of 1500 m to 2500 m. This suggests that the cap rock of the Pukou Formation in the study area has good sealing ability.
Through geological suitability evaluation, ground suitability evaluation, and economic evaluation of the pool, the suitability of the power plant is divided into 5 levels using the method of multi-source information overlay processing, and finally, suitable sites for CO2 storage in coal-fired power plants are selected.
The evaluation results indicate that the suitability of the surrounding sites of Huaiyin Power Plant is mainly divided into two levels (i.e., relatively suitable, generally suitable), and the area in the generally suitable level accounts for more than 80% (Figure 3). The suitable sites are mainly distributed in the northeast, central, and southwest of the study area, which are basically consistent with the depression position, and the central part is the most suitable area. According to the evaluation results of CO2 saline water layer storage site selection, one storage target area with good suitability around Huaiyin Power Plant for simulation research was selected (Figure 3). The actual storage site area is 25.00 km2 (the evaluation model area is 7.5 km × 7.5 km = 56.25 km2, including 5 km × 5 km distribution range of the site). The reservoir and cap rocks mainly include the member 2 and 3 sections of Pukou Formation (i.e., Kp3 and Kp2). There are no fault cuts around the target storage site, and the strata are flat here.

4. Evaluation Method of Water Displacement Potential

4.1. Simulation Program

Since the early 1990s, scholars have established many CO2 geological storage potential assessment methods for specific problems and assessment scales [27,28,32,33]. In particular, the calculation formulas of the United States Department of Energy and the Carbon Sequestration Leadership Forum (CSLF) are relative scientific. According to the calculation method for CO2 geological storage in pure saline water layers proposed by USDOE, potential assessment of CO2 geological storage is mainly achieved by estimating the volume of underground storage space under the premise that the storage space must meet the site selection criteria. However, the geological storage and displacement potential of CO2 deep salt water layers is closely related to the CO2 storage capacity. The theoretical evaluation method for CO2 water displacement potential is similar to the CO2 oil displacement potential evaluation method. It is generally estimated by multiplying the geological storage capacity of CO2 by the displacement efficiency of deep saline water (Equations (1) and (2)).
G C O 2 = A · h · φ e · ρ C O 2 · E s a l i n e
G W a t e r = G C O 2 · E R e c o v e r y
where A is the area of reservoir distribution, h is the reservoir thickness, φ e is the average effective porosity of salt water layer,   ρ C O 2 is the density of CO2 in temperature and pressure conditions of the saline water layer, E s a l i n e is the Storage efficiency (effective coefficient), and E R e c o v e r y is the displacement coefficient of deep saline water. For the evaluation of predicted displacement potential, the salt water displacement coefficient is generally taken as 1.0, which means that the displacement efficiency of carbon dioxide and deep salt water is 1:1 (mass).
Based on selected evaluation area, the numerical simulation method is adopted to evaluate the CO2 flooding potential. Firstly, a geological model of the evaluation site is constructed. And then, the plans of different injection and extraction were set. Finally, the prediction of water flooding potential of CO2-EWR technology was carried out.

4.2. Conceptual Model

The evaluation method for CO2 geological storage and water displacement potential is mainly based on basin basic geological research, static geological modeling, and the application of numerical simulation technology to conduct the dynamic evaluation of CO2 geological storage potential under different scenarios. The reservoir modeling is the fundamental of the entire evaluation process, which may direct determine the quality of the evaluation results. Based on the geological model, the factors such as fluid flow, component material balance, and water-rock reaction are taken in to consider in the evaluation of the potential for geological storage and water displacement potential of CO2 in deep salt water layer. In addition, the impacts of injection method, injection, and extraction well layout on water repulsion efficiency are also been focused during the evaluation process. An important result of numerical simulation is to provide the maximum water displacement potential during the CO2 geological storage process of the site, and to provide the best injection and extraction plan, which has important engineering reference significance. However, the study area is currently in the pre-feasibility stage. Due to the lack of core data, A simplified homogeneous geological model was established in the study. Compared with the heterogeneous model, the total amount of CO2 injection in the homogeneous model is significantly increased due to the influence of reservoir heterogeneity on the formation of CO2 migration channels. So, the discussion of CO2-EWR technology with different production/injection well ratios (PIR) is the focus of this research.

4.2.1. Model Building

The model is simulated and analyzed using ECO2N module on the TOUGH2 software, which has high stability and reliability during the numerical simulation process in the condition of homogeneous media. 3D geological modeling was conducted on the selected sites of Kp3 and Kp2 sections. Using the top and bottom elevations collected from drilling data, the strata were specifically divided into four sets of reservoir-cap combinations. Based on the assumption that the site strata are generalized as horizontal strata, the geological model range was set to X: 0 m~7500 m, Y: 0 m~7500 m, and Z: −1100 m~−2500 m. The formation thickness is 1400 m, and the sand to soil ratio is 0.47. The cube grid generation method was used, with 50 grids in the X and Y directions and 25 grids in the Z direction, for a total of 62,500 grids in the model (Figure 4). The boundary condition is set as a closed boundary.

4.2.2. Model Parameter Settings

The stratigraphic parameters were assigned values with reference to the actual information acquired at the site. The formation is set at a uniform temperature of 55 ℃. Based on the analysis and division of formation parameters, the formation was divided into 8 layers for simulation. As shown in Table 2, the single-layer porosity and permeability were assigned based on the average porosity and permeability data of the corresponding layers (Figure 5). The formation pressure is calculated as follows:
P = 1.013 × 105 − 104 × Z
where P is formation pressure, Z is the depth.

5. Numerical Simulation Analysis

5.1. Scenario Settings

In the water displacement potential evaluation, different production/injection well ratios (PIR) have been set up (i.e., 1 injection well and 1 production well (PIR is 1), 1 injection well and 2 production wells (PIR is 2), and 1 injection well and 4 production wells (PIR is 4)) (Table 3, Figure 6). The injection wells utilize constant flow and constant speed injection methods. Three different injection rate schemes have been designed: 0.5 million tons/year, 1 million tons/year, and 2 million tons/year. The bottom pressure of the production well was set at a constant value of 19.6 MPa. The production index is 4 × 10−12 m³, and the gradient is set to 3. Different PIR scenarios were continuously running for 100 years to evaluate the water displacement potential of CO2.

5.2. Evaluation

The combination of CO2 geological storage and deep salt water extraction could enhance storage safety while obtaining substantial groundwater resources. This evaluation examined multiple options for water displacement potential evaluation. The problems that may be encountered in actual engineering were taken into consideration. Specifically, research works in three aspects (i.e., the CO2 spatial distribution, reservoir pressure changes, and cap rock sealing) were conducted.

5.2.1. CO2 Spatial Distribution in Different Scenarios

Different CO2 injection schemes can form different spatial distribution characteristics of CO2. Figure 7, Figure 8, Figure 9, Figure 10, Figure 11, Figure 12, Figure 13, Figure 14 and Figure 15 show the spatial distribution of CO2 after 30, 50, 70, and 100 years of simulation for three PIR scenarios. At the same injection rate (Figure 7, Figure 10 and Figure 13), the CO2 plume is asymmetrically distributed under the scenarios of PIR = 1, while the CO2 plume is symmetrically distributed under the schemes of PIR = 2 and PIR = 4. This is due to the influence of the pressure difference, and the CO2 plume will preferentially expand in the direction of the production well, indicating that the distribution of the production wells will affect the spatial distribution of the CO2, which in turn affects the amount of CO2 trapped.
Through comparison, it can be found that make the PIR = 1 with injection rate of 0.5 million tons/year as an exception, the CO2 plume boundary has all reached the location of the extraction well after 100 years of continuous operation in other design schemes. As shown in Figure 16, with the same PIR, a higher injection rate results in a shorter time for the CO2 plume to reach the production wells. This suggests that a higher injection rate can improve CO2 storage efficiency. Additionally, with the same injection rate, the time for the CO2 plume to reach the production wells is inversely proportional to the number of production wells, indicating that increasing the number of production wells can lead to greater CO2 storage.

5.2.2. Reservoir Pressure Changes in Different Scenarios

Figure 17 illustrates the change in injection well pressure with time under different injection scenarios. It can be seen that the trend of reservoir pressure change is the same under different scenarios. Initially, the reservoir pressure increases rapidly. As salt water is extracted by the production wells, the pressure of injection well gradually decreases and then tends to stabilize. Subsequently, there is an increasing trend of reservoir pressure. The fixed operating conditions for 50 years demonstrate that the stable injection pressures are 28.44 MPa, 25.87 MPa and 24.58 MPa for the scenarios PIR = 1, PIR = 2 and PIR = 4, respectively. So with the increase in the number of production wells, the reservoir pressure decreases, indicating that the increase in the number of extraction wells has significantly reduced reservoir pressure and the risk of CO2 leakage. As shown in Figure 17, When the PIR = 1, the reservoir pressure began to rise rapidly after sixty years of CO2 injection. This could be attributed to the fact that pressure build-up from CO2 sequestration cannot be effectively reduced by relying on only one production well. While the PIR = 3, Reservoir pressure can eventually maintain a stable value as injection time increases. Therefore, when the PIR is low, prolonged CO2 injection may cause the reservoir pressure to rise, potentially causing CO2 to leak if the cap breaks.

5.2.3. Sealing of Cap Rock under Different Scenarios

The storage capacity of the system is primarily limited by the time required for the CO2 plume to reach the production wells. As shown in Figure 16 and Figure 18, with the injection rate of 1 million tons per year, the free CO2 gas appears in the production wells after approximately 61, 54, 53 years under different PIR conditions, which implies that CO2 will begin to leak as the continue exploitation of deep saline water. Thus, under the premise of restricted system storage capacity, it was found that the time for the CO2 plume to reach the production wells decrease as the increase in production wells number. It is indicated that CO2 can be injected for shorter periods of time with the PIR increases.
Figure 19 displays the vertical saturation of CO2 within the Injection well at the point of cap rock breakthrough in different injection scenarios under the premise of unrestricted system storage capacity. The vertical gas saturation of different scenarios basically coincides when the CO2 plume reaches the production wells, with only differences in breakthrough time. It is also shown that the gas saturation is increased with the increase in the number of the production well, which demonstrates that increasing the number of production wells can lead to greater CO2 storage. As shown in Figure 20, during cap rock breakthrough, the CO2 injection volume is 61 million tons, 80 million tons, and 95 million tons, respectively, for the scenarios of PIR = 1, PIR = 2 and PIR = 4. The total water production of the production wells is 102 million tons, 95.9 million tons, and 74.3 million tons, respectively. So, When PIR = 4, the total CO2 injection increased by 55.73% compared to PIR = 1. The CO2 displacement saltwater coefficients are 1.67, 1.20, and 0.78, respectively. Thus, under the premise of unrestricted system storage capacity, when a cap rock breakthrough (leakage) occurs, the amount of CO2 injection increases and the total amount of water extracted decreases as the increase in production wells. Although increasing the PIR reduces the total time of CO2 injection, it also increases the total amount of CO2 injected. As the PIR increases, however, total water production decreases. As previously mentioned, a lower number of producing wells leads to increased reservoir pressures during extended CO2 injection. Consequently, higher PIRs lead to greater returns.

6. Conclusions

Based on the multi-source information superposition evaluation technology, the potential target areas of CO2 saline water storage and water displacement are evaluated and optimized in Huaiyin Sag. Then, the potential of the application of CO2-EWR technology is evaluated by numerical simulation, and the spatial distribution of CO2, reservoir pressure change and cap sealing under different scenarios are discussed. The main conclusions are as follows:
(1) Considering various factors including regional geology, reservoir cap rock combination, and physical parameters in the study area, and following principles of the assessment for site selection of CO2 saline water reservoir storage, the suitability of the surrounding area of Huaiyin Power Plant is divided into two levels: relatively suitable and generally suitable, in which the general suitable area accounts for over 80%.
(2) Different CO2 injection schemes can result in different spatial distribution characteristics of CO2. The CO2 storage capacity of a site increases with the number of production wells, while maintaining the same injection rate. The higher the injection rate is, the faster the CO2 plume expands.
(3) When CO2 is injected into the formation, the reservoir pressure experiences a rapid increase followed by a decrease, and then another increase. The changes in reservoir pressure in different scenarios indicate that the higher the number of production wells, the lower the stable injection pressure.
(4) It was found that increasing the number of production wells leads to a shorter time for the CO2 plume to reach them. Under the premise of unrestricted system storage capacity, when a cap rock breakthrough (leakage) occurs, the amount of CO2 injection increases and the total amount of water extracted decreases as the increase in production wells. This also results in a smaller coefficient of CO2 displacement for saline.

Author Contributions

Conceptualization, C.Z.; formal analysis, C.Z.; methodology, C.Z., X.M. and T.L.; software, C.Z., L.F. and S.W.; validation, C.Z. and Y.D.; investigation, C.Z., L.F. and T.L.; data curation, C.Z., X.M. and T.L.; writing—original draft preparation, C.Z.; writing—review and editing, C.Z. and L.F.; proj administration, C.Z.; funding acquisition, C.Z. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the National Natural Science Foundation of China (No.42141013), Qinghai Province Science and Technology Application Basic Research Project (No.2022-ZJ-735), China Geological Survey Project (No. DD20221818 and DDDD20242531).

Data Availability Statement

The data presented in this study are available on request from the corresponding author.

Acknowledgments

I would like to extend my appreciation to my wife Yanhuan Zhao, for providing all necessary support to conduct this research work.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Zhao, L.; Pan, W.B.; Lin, H. Can Fujian Achieve Carbon Peak and Pollutant Reduction Targets before 2030? Case Study of 3E System in Southeastern China Based on System Dynamics. Sustainability 2022, 14, 11364. [Google Scholar] [CrossRef]
  2. Fortuńsk, B. Sustainable Development and Energy Policy: Actual CO2 Emissions in the European Union in the Years 1997–2017, Considering Trade with China and the USA. Sustainability 2020, 12, 3363. [Google Scholar] [CrossRef]
  3. McGeough, E.J.; Litlte, S.M.; Janzen, H.H.; McGinn, S.M.; Beauchemin, K.A. Life-cycle assessment of greenhouse gas emissions from dairy production in Eastern Canada: A case study. J. Dairy Sci. 2012, 95, 5164–5175. [Google Scholar] [CrossRef]
  4. Dalgaard, T.; Olfsen, J.E.; Petersen, S.O.; Jørgensen, U.; Kristensen, T. Developments in greenhouse gas emissions and net energy use in Danish agriculture—How to achieve substantial CO2 reductions? Environ. Pollut. 2011, 159, 3193–3203. [Google Scholar] [CrossRef]
  5. Chaudhry, R.; Fischlein, M.; Larson, J.; Hall, D.M.; Peterson, T.R.; Wilson, E.J.; Stephen, J.C. Policy stakeholders’ perceptions of carbon capture and storage: A comparison of four US states. J. Clean. Prod. 2013, 52, 21–32. [Google Scholar] [CrossRef]
  6. Tolon Becherya, A.; Perez-Martinez, P.; Lastra Bravo, X. A methodology for territorial distribution of CO2 emission reductions in transport sector. Int. J. Energy Res. 2012, 36, 1298–1313. [Google Scholar] [CrossRef]
  7. Scott, V.; Gilfillan, S.; Markusson, N.; Chalmers, H.; Haszeldine, R.S. Last chance for carbon capture and storage. Nat. Clim. Chang. 2012, 3, 105–111. [Google Scholar] [CrossRef]
  8. Bachu, S.; Adams, J.J. Sequestration of CO2 in geological media in response to climate change: Capacity of deep saline aquifers to sequester CO2 in soution. Energy Convers. Manag. 2003, 44, 3151–3175. [Google Scholar] [CrossRef]
  9. Li, X.C.; Liu, Y.F.; Bai, B.; Fang, Z. Ranking and screening of CO2 saline aquifer storage zones in China. Chin. J. Rock Mech. Eng. 2006, 25, 963–968. [Google Scholar]
  10. Kong, W.Z.; Bai, B.; Li, X.C.; Ning, W. Sealing Efficiency of Combined Caprock for CO2 Storage in Saline aquifer. Chin. J. Rock Mech. Eng. 2015, A1, 2671–2678. [Google Scholar]
  11. Zhou, Y.B.; Wang, R.; He, Y.F.; Zhao, S.X.; Zhou, Y.L.; Zhang, Y. Analysis and comparison of typical cases of CO2 geological storage in saline aquifer. Pet. Geol. Recovery Effic. 2023, 30, 162–167. [Google Scholar]
  12. Liu, S.Q.; Huang, F.S.; Du, R.B. Progress and typical case analysis of demonstration projects of the geological sequestration and utilization of CO2. Coal Geol. Explor. 2023, 51, 158–174. [Google Scholar]
  13. Tapia, J.F.D.; Lee, J.Y.; Ool, R.E.H.; Foo, D.C.Y.; Tan, R.R. Optimal CO2 allocation and scheduling in enhanced oil recovery (EOR) operations. Appl. Energy 2016, 184, 337–345. [Google Scholar] [CrossRef]
  14. Zhang, E.Y. Introduction to the CO2 geosequestration demonstration project in the Otway basin in Australia. Hydrogeol. Eng. Geol. 2012, 39, 131–137. [Google Scholar]
  15. Bachu, S.; Bonijoly, D.; Bradshaw, R.J.; Burruss, R.; Holloway, S.; Christensen, N.P.; Mathiassen, O.M. CO2 storage capacity estimation: Methodology and gaps. Int. J. Greenh. Gas Control 2007, 1, 430–443. [Google Scholar] [CrossRef]
  16. Xu, T.F.; Pruess, K.; Apps, J. Numerical studies of fluid rock interactions in Enhanced Geothermal Systems (EGS) with CO2 as working fluid. In Proceedings of the Thirty-Third Workshop on Geothermal Reservoir Engineering, Stanford, CA, USA, 28–30 January 2008. [Google Scholar]
  17. Zhang, W.; Lv, P. Density-driven convection in carbon dioxide geological storage: A review. Hydrogeol. Eng. Geol. 2013, 40, 101–107. [Google Scholar]
  18. Desilva, P.N.K.; Ranjith, P.G. A study of methodologies for CO2 storage capacity estimation of saline aquifers. Fuel 2012, 93, 13–27. [Google Scholar] [CrossRef]
  19. Ma, X.; Li, X.F.; Yang, G.D.; Huang, W.; Diao, Y.J.; Hu, L.S.; Zhang, H.; Wei, S. Study on field-scale of CO2 geological storage combined with saline water recovery: A case study of east Junggar basin of Xinjiang. Energy Procedia 2018, 154, 36–41. [Google Scholar] [CrossRef]
  20. Vilarrasa, V.; Bolster, D.; Olivella, S.; Carrera, J. Coupled hydromechanical modeling of CO2 sequestration in deep saline aquifers. Int. J. Greenh. Gas Control. 2010, 4, 910–919. [Google Scholar] [CrossRef]
  21. Li, Q.; Wei, Y.N. Progress in combination of CO2 geological storage and deep saline water recovery. Sci. Technol. Rev. 2013, 31, 65–70. [Google Scholar]
  22. Bergmo, P.E.S.; Grimstad, A.A.; Lindeberg, E. Simultaneous CO2 injection and water production to optimise aquifer storage capacity. Int. J. Greenh. Gas Control 2011, 5, 555–564. [Google Scholar] [CrossRef]
  23. Yang, G.D.; Li, Y.L.; Ma, X.; Aleks, A.; Hao, N. Modeling study of enhanced thermal brine extraction using supercritical CO2. Geol. Sci. Technol. Inf. 2014, 33, 233–240. [Google Scholar]
  24. Li, Q.; Wei, Y.N.; Liu, G.Z.; Lin, Q. Combination of CO2 geological storage with deep saline water recovery in Western China: Insights from numerical analyses. Appl. Energy 2014, 116, 101–110. [Google Scholar] [CrossRef]
  25. Wang, R.; Li, Y.; Lv, C.Y.; Tang, Y.Q.; Cui, M.L.; Jia, H.C.; Liu, X.; Liu, J.D. Study on potential evaluation method on CO2-EWR and storage for deep saline layers in Ordos Basin. Unconv. Oil Gas 2021, 8, 50–55. [Google Scholar]
  26. Heath, J.E.; Mckenna, S.A.; Dewers, T.A.; Roach, J.D.; Kobos, P.H. Multiwell CO2 injectivity: Impact of boundary conditions and brine extraction on geologic CO2 storage efficiency and pressure buildup. Environ. Sci. Technol. 2014, 48, 1067–1074. [Google Scholar] [CrossRef]
  27. Buscheck, T.A.; Sun, Y.W.; Hao, Y.; Wolery, T.J.; Bourcier, W.; Tompson, A.F.B.; Jones, E.D.; Friedmann, S.J.; Alines, R.D. Combining brine extraction, desalination, and residual-brine reinjection with CO2 storage in saline formations: Implications for pressure management, capacity, and risk mitigation. Energy Procedia 2011, 4, 4283–4290. [Google Scholar] [CrossRef]
  28. He, B.; Xu, T.F.; Yuan, Y.L.; Tian, H.L.; Hou, Z.Y.; Wang, F.G. An analysis of the influence factors on CO2 injection capacity in a deep saline formation: A case study of Shiqianfeng Group in the Erdos Basin. Hydrogeol. Eng. Geol. 2016, 1, 136–142. [Google Scholar]
  29. Zhang, Z.X.; Xie, J.; Qi, J.H.; Hu, L.T.; Zhang, K.N.; Wu, L.Z. Numerical simulation of CO2 leakage along faults from geologic carbon dioxide sequestration. Hydrogeol. Eng. Geol. 2018, 45, 109–116. [Google Scholar] [CrossRef]
  30. Hu, Z.K.; Li, Y.; Suo, R.T. Effects of CO2 Purity on Residual Water During Carbon Sequestration in Deep Saline Aquifers. Geol. J. Univ. 2023, 1, 57–65. [Google Scholar]
  31. Fang, Q.; Li, Y.L. Exhaustive brine production and complete CO2 storage in Jianghan Basin of China. Environ. Earth Sci. 2014, 72, 1541–1553. [Google Scholar] [CrossRef]
  32. Liu, D.Q.; Agarwal, R.; Li, Y.L. Numerical simulation and optimization of CO2-enhanced water recovery by employing a genetic algorithm. J. Clean. Prod. 2016, 133, 994–1007. [Google Scholar] [CrossRef]
  33. Trujillo, N.; Rose-Coss, D.; Heath, J.; Dewers, T.; Ampomah, W.; Mozley, P.; Cather, M. Multiscale Assessment of Caprock Integrity for Geologic Carbon Storage in the Pennsylvanian Farnsworth Unit, Texas, USA. Energies 2021, 14, 5824. [Google Scholar] [CrossRef]
  34. Li, Y.; Huang, W.H.; Jin, Y.; He, Y.F.; Chen, Z.H.; Tang, Y.; Wu, G.Y. Different reservoir types of CO2 flooding in Sinopec EOR technology development and application under “dual carbon” vision. Pet. Reserv. Eval. Dev. 2021, 11, 793–804. [Google Scholar]
  35. Chen, Z.H.; Wu, G.Y.; Qian, W.M.; Wang, J.; Ma, T.; Wang, H.M.; Zheng, Y.W.; Xiong, X.Y. EOR technology and application of CO2 injection for small complex fault block reservoirs in Subei Basin. Pet. Geol. Recovery Effic. 2020, 27, 152–162. [Google Scholar]
  36. Cao, M.L.; Chen, J.P. The site selection geological evaluation of the CO2 storage of the deep saline aquifer. Acta Geol. Sin. 2022, 96, 1868–1882. [Google Scholar]
  37. Diao, Y.J.; Zhang, S.Q.; Guo, J.Q.; Li, X.F.; Fan, J.J.; Jia, X.F. Reservoir and caprock evaluation of CO2 geological storage site selection in deep saline aquifers. Rock Soil Mech. 2012, 8, 242–2428. [Google Scholar]
  38. Liu, Z.J.; Shi, J.G.; Zhang, Y. Recent advances in storage technology of carbon dioxide. Sino-Glob. Energy 2017, 22, 1–9. [Google Scholar]
  39. Evans, A.D.; Takeshi, K.; Ronny, P. Avinoam Rabinovich Estimating Three-Dimensional Permeability Distribution for Modeling Multirate Coreflooding Experiments. Sustainability 2023, 15, 3148. [Google Scholar]
  40. Goodman, A.; Sanguinito, S.; Tkach, M. Investigatingthe role of water on CO2-Utica shale interactions for carbon storage and shale gasextraction activities-evidence for pore scale alterations. Fuel 2019, 242, 744–755. [Google Scholar] [CrossRef]
  41. Diao, Y.J.; Ma, X.; Li, X.F.; Zhang, C.L.; Liu, T. Evaluation methods of underground space utilization for CO2 geological storage in deep saline aquifers. Geol. Surv. China 2021, 8, 87–91. [Google Scholar]
  42. Li, Y. Carbon Neutralization and Advances in Carbon Capture, Utilization and Storage Technology; China Petrochemical Press: Beijing, China, 2021; Volume 9. [Google Scholar]
  43. Dong, X.J. The Stability Evaluation of Goaf Based on the multi-source information fusion technology. Min. Res. Dev. 2017, 37, 100–105. [Google Scholar]
  44. Zou, W.; Liu, B.; Sun, Q. Survey of Key Technologies on Efficiency Evaluation of Information Fusion System with Multiple Sources. Comput. Digit. Eng. 2010, 3, 1–6. [Google Scholar]
Figure 1. Location and geological structures in the study area, Huaiyin Sag, Subei Basin, East China. (a). Structural map of Subei Basin; (b). Structural map of Huaiyin Sag.
Figure 1. Location and geological structures in the study area, Huaiyin Sag, Subei Basin, East China. (a). Structural map of Subei Basin; (b). Structural map of Huaiyin Sag.
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Figure 2. Stratigraphic column of the Huaiyin Sag.
Figure 2. Stratigraphic column of the Huaiyin Sag.
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Figure 3. Site selection evaluation of saline water layer storage site.
Figure 3. Site selection evaluation of saline water layer storage site.
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Figure 4. Schematic diagram of grid division of the research site model. (a) Top view of the model; (b) Side view of the model.
Figure 4. Schematic diagram of grid division of the research site model. (a) Top view of the model; (b) Side view of the model.
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Figure 5. Geological model of the proposed evaluation site.
Figure 5. Geological model of the proposed evaluation site.
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Figure 6. Well location distribution and different production/injection well ratios (PIR): (a) 1 injection well and 1 production well (PIR is 1); (b) 1 injection well and 2 production wells (PIR is 2); (c) 1 injection well and 4 production wells (PIR is 4).
Figure 6. Well location distribution and different production/injection well ratios (PIR): (a) 1 injection well and 1 production well (PIR is 1); (b) 1 injection well and 2 production wells (PIR is 2); (c) 1 injection well and 4 production wells (PIR is 4).
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Figure 7. Distribution of CO2 plume under the scenario of PIR = 1 with an injection rate of 0.5 million tons/year.
Figure 7. Distribution of CO2 plume under the scenario of PIR = 1 with an injection rate of 0.5 million tons/year.
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Figure 8. Distribution of CO2 plume under the scenario of PIR =1 with an injection rate of 1 million tons/year.
Figure 8. Distribution of CO2 plume under the scenario of PIR =1 with an injection rate of 1 million tons/year.
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Figure 9. Distribution of CO2 plume under the scenario of PIR = 1 with an injection rate of 2 million tons/year.
Figure 9. Distribution of CO2 plume under the scenario of PIR = 1 with an injection rate of 2 million tons/year.
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Figure 10. Distribution of CO2 plume under the scenario of PIR = 2 with an injection rate of 0.5 million tons/year.
Figure 10. Distribution of CO2 plume under the scenario of PIR = 2 with an injection rate of 0.5 million tons/year.
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Figure 11. Distribution of CO2 plume under the scenario of PIR = 2 with an injection rate of 1 million tons/year.
Figure 11. Distribution of CO2 plume under the scenario of PIR = 2 with an injection rate of 1 million tons/year.
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Figure 12. Distribution of CO2 plume under the scenario of PIR = 2 with an injection rate of 2 million tons/year.
Figure 12. Distribution of CO2 plume under the scenario of PIR = 2 with an injection rate of 2 million tons/year.
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Figure 13. Distribution of CO2 plume under the scenario of PIR = 4 with an injection rate of 0.5 million tons/year.
Figure 13. Distribution of CO2 plume under the scenario of PIR = 4 with an injection rate of 0.5 million tons/year.
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Figure 14. Distribution of CO2 plume under the scenario of PIR = 4 with an injection rate of 1 million tons/year.
Figure 14. Distribution of CO2 plume under the scenario of PIR = 4 with an injection rate of 1 million tons/year.
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Figure 15. Distribution of CO2 plume under the scenario of PIR = 4 with an injection rate of 2 million tons/year.
Figure 15. Distribution of CO2 plume under the scenario of PIR = 4 with an injection rate of 2 million tons/year.
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Figure 16. The time of CO2 plume reaching the recovery well under different scenarios.
Figure 16. The time of CO2 plume reaching the recovery well under different scenarios.
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Figure 17. Changes in injected reservoir pressure under different scenarios.
Figure 17. Changes in injected reservoir pressure under different scenarios.
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Figure 18. Distribution of CO2 plumes when CO2 gas appears in the production wells under different scenarios. (a) PIR = 1; (b) PIR = 2; (c) PIR = 4.
Figure 18. Distribution of CO2 plumes when CO2 gas appears in the production wells under different scenarios. (a) PIR = 1; (b) PIR = 2; (c) PIR = 4.
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Figure 19. Gas saturation of Injection well when CO2 plume reaches mining well.
Figure 19. Gas saturation of Injection well when CO2 plume reaches mining well.
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Figure 20. The injection volume and water production in different PIR.
Figure 20. The injection volume and water production in different PIR.
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Table 1. The feasibility evaluation of CO2 saline water storage (revised from Cao et al. [37]).
Table 1. The feasibility evaluation of CO2 saline water storage (revised from Cao et al. [37]).
BasisParameterStandardHuayin Sag
geotectonics Sedimentary basins in stable continental interior or near stable continental plate interiorContinental rift basin
Volume conditionsbasin area≥2500 Km2/
reservoir thickness>20 mKp2: 60–115 m
Kp3: 230–250 m
tectonic featurestrataThe occurrence is gentle, stable and has lateral sealing property/
foldTop of the anticlineJianhu Uplift
faultNo fault, less fault or good fault sealingTanlu Fault
Huaiyin-Xiangshui Fault
reservoir conditiondepth>800 m1100–2500 m
physical propertyThe porosity is generally greater than 10%, and there is no absolute requirement for permeability.Kp2: 5.38%
Kp3: 6.82%
reservoir pressureExceeding the CO2 critical pressure (7.5 MPa)25 MPa
geothermal conditiongeothermal gradientThe lower the more favorable/
geothermal temperature≥35 °C55 °C
local stabilityearthquake volcano or active faultEarthquakes, volcanoes, and active faults are not developedNo
cap rock conditioncaprock thickness>100 mKp2: 125–130 m
Kp3: 340 m
Table 2. Setting of formation porosity and permeability parameters.
Table 2. Setting of formation porosity and permeability parameters.
FormationReservoir Cap RockLaminationTop Buried Depth mThickness mPorosityPermeability mD
Kp3Caprocklayer1−11004000.010.1
Reservoirlayer2−1500600.0546.65
Caprocklayer3−15601250.010.1
Reservoirlayer4−16851150.0546.65
Caprocklayer5−18001300.010.1
Kp2ReservoirLayer6−19302300.0618.9
CaprockLayer7−2160900.010.1
ReservoirLayer8−22502500.0618.9
Note: Layers 2–8 refer to the injection and extraction intervals.
Table 3. Scenario settings of injection.
Table 3. Scenario settings of injection.
Order NumberProduction/Injection Well Ratio (PIR)Injection and Extraction Spacing (km)Injection Rate (10,000 tons/year)Pumping Pressure (MPa)Pumping Time
Case 112 km5020.2100 yr
Case 112 km10020.2100 yr
Case 112 km20020.2100 yr
Case 222 km5020.2100 yr
Case 222 km10020.2100 yr
Case 222 km20020.2100 yr
Case 342 km5020.2100 yr
Case 342 km10020.2100 yr
Case 342 km20020.2100 yr
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Zhang, C.; Diao, Y.; Fu, L.; Ma, X.; Wang, S.; Liu, T. Evaluation of the Potential for CO2 Storage and Saline Water Displacement in Huaiyin Sag, Subei Basin, East China. Processes 2024, 12, 547. https://doi.org/10.3390/pr12030547

AMA Style

Zhang C, Diao Y, Fu L, Ma X, Wang S, Liu T. Evaluation of the Potential for CO2 Storage and Saline Water Displacement in Huaiyin Sag, Subei Basin, East China. Processes. 2024; 12(3):547. https://doi.org/10.3390/pr12030547

Chicago/Turabian Style

Zhang, Chenglong, Yujie Diao, Lei Fu, Xin Ma, Siyuan Wang, and Ting Liu. 2024. "Evaluation of the Potential for CO2 Storage and Saline Water Displacement in Huaiyin Sag, Subei Basin, East China" Processes 12, no. 3: 547. https://doi.org/10.3390/pr12030547

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