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Article

CO2 Storage Site Analysis, Screening, and Resource Estimation for Cenozoic Offshore Reservoirs in the Central Gulf of Mexico

1
Spears School of Business, Oklahoma State University, Stillwater, OK 74078, USA
2
School of Chemical Engineering, Oklahoma State University, Stillwater, OK 74078, USA
3
Boone Pickens School of Geology, Oklahoma State University, Stillwater, OK 74078, USA
*
Author to whom correspondence should be addressed.
Energies 2024, 17(6), 1349; https://doi.org/10.3390/en17061349
Submission received: 29 December 2023 / Revised: 2 February 2024 / Accepted: 1 March 2024 / Published: 12 March 2024
(This article belongs to the Special Issue Coal, Oil and Gas: Lastest Advances and Propects)

Abstract

:
The storage potential of hydrocarbon reservoirs in the central Gulf of Mexico (GOM) makes future development of CO2 storage projects in those areas promising for secure, large-scale, and long-term storage purposes. Focusing on the producing and depleted hydrocarbon fields in the continental slope of the central GOM, this paper analyzed, assessed, and screened the producing sands and evaluated their CO2 storage potential. A live interactive CO2 storage site screening system was built in the SAS® Viya system with a broad range of screening criteria combined from published studies. This offers the users a real-time assessment of the storage sites and enables them to adjust the filters and visualize the results to determine the most suitable filter range. The CO2 storage resources of the sands were estimated using a volumetric equation and the correlation developed by the National Energy Technology Laboratory (NETL). The results of this study indicate that 1.05 gigatons of CO2 storage resources are available in the developed reservoirs at the upper slope area of the central GOM. The Mississippi Canyon and Green Canyon protraction areas contain the fields with the largest storage resources.

1. Introduction

As part of the Regional Carbon Storage Partnership program sponsored by the U.S. Department of Energy (DOE), the Southeast Regional Carbon Storage Partnership (SECARB) focuses on large-scale, long-term CO2 injection and storage evaluation within the southeast United States. An earlier study, the Southeastern Offshore Storage Resource Assessment (SOSRA), assessed the Eastern Gulf and the easternmost portion of the Central Gulf, including two other planning areas: the Mid-Atlantic and the South-Atlantic. Significant advances in knowledge and technology were made in their research for the assessment and quantitative determination of offshore CO2 storage resources in the SOSRA region, which paved the way for commercialization [1].
Previous detailed studies have shed light on multi-phase tectonic history, salt tectonics, stratigraphic and structural petroleum trapping, and multi-stage petroleum systems in the Eastern and Central GOM planning areas [2,3,4,5,6]. Storage potential was also estimated, and more than 100 gigatons of CO2 storage potential were identified in the continental shelf offshore of Mississippi, Alabama, and Florida [6,7,8]. However, the storage potential of the active and depleted hydrocarbon fields in the central GOM, continental shelf, and continental slope offshore of Louisiana is still largely unknown, and the suitability of the fields for long-term CO2 storage is yet to be investigated.
Oil fields are maturing in the Gulf of Mexico’s continental slope, and several fields are undergoing water floods [9,10,11]. As these fields mature further, advancing to CO2-enhanced oil recovery may be a viable solution to prolong the life of the fields. The goal of this DOE-funded study is to carry out a high-level assessment of the suitability of the active and depleted fields in the continental slope region of the central GOM for CO2 storage and estimate the volume of CO2 that can be stored in the reservoirs on a field-by-field and reservoir-by-reservoir basis. This involves analyzing the subsurface conditions of the fields in the study area, identifying and modifying screening criteria, and applying them to locate potential storage sites. To ease the process of collecting, processing, and analyzing a large volume of geological and production data from the study area and creating user interactive visualizations that provide insights on the potential CO2 storage sites in the study area, an online cloud platform called SAS® Viya was utilized. SAS® Viya (V.03.05) provides software-driven decision support systems that are well-suited for multi-source, multi-variate, data mining and data analytics problems related to geologic CO2 storage projects [12], and the use of this software is novel and can be applied to geologic storage problems in sedimentary basins around the world. This online cloud platform also provides a comprehensive solution to integrate different data sources and discover new insights with quick analytics and visualization.
In the scope of this study, the major geological characteristics of continental slope areas of the central GOM were examined and compared to define the appropriate reservoir screening criteria, drawing on the experience of previous regional CO2 storage assessment and screening studies [13,14,15]. The 2018 Sands Atlas, published online by the Bureau of Ocean Energy Management (BOEM), was the primary data source used to analyze the study area. A live and interactive CO2 storage site screening system was built in the SAS® Viya platform that allows users to change the criteria to screen and visualize the locations of potential reservoirs quickly in the central GOM. In addition, ArcGIS® Pro was used as a supplementary tool for geospatial analysis and analysis of geological features.
High-level estimation of CO2 storage resources of the reservoirs in the study area is also provided using the static volumetric equations from Smith et al. [15] and the National Energy Technology Laboratory (NETL) [16]. The density of CO2 under reservoir conditions was estimated as a function of pressure and temperature using the correlation developed by Bikkina et al. [17] and incorporated in the storage estimation. These estimations are used in the SAS® Viya system to identify fields with the optimum CO2 storage resource.
It should be noted that the estimation of CO2 storage resources should also include current economic and regulatory considerations [16]. Even though deepwater fields in the eastern portion of the study area were prioritized in storage estimation due to their proximity to the Mississippi Delta shoreline and the associated infrastructure, assessing factors such as the cost of operation, transport to the storage site, injection, and well maintenance is beyond the scope of this study and not considered in the estimation. Thus, according to the CO2 Storage Resources Management System (SRMS) guidelines by Society of Petroleum Engineer (SPE) (SPE) [18], the estimated storage potential falls into the category of contingent storage resource and is assumed to be equal to the SRMS storage capacity until more information about the regulatory logistics and economic feasibility of offshore storage operations becomes available.

2. Study Area

The active and depleted oil and gas reservoirs in the GOM are located in federal offshore areas off the southeast coasts of Texas, Louisiana, Mississippi, Alabama, and Florida. There are 1317 unique fields and 13,380 sands reported in the 2018 BOEM Sands Atlas database, out of which 862 fields (5500 sands) are depleted. This study focuses only on the active and depleted oil and gas fields in the central GOM, including all federal and state waters east of the Lafayette District to the Mobile and Viosca Knoll areas at the eastern boundary (Figure 1).
From the offshore Louisiana continental shelf to the upper continental slope, the study area was classified into shelf and slope zones. The study area includes 672 unique fields and 7496 data points from reservoir sands. In the region, 509 fields (6537 sands) are in the shelf region, and 163 fields (956 sands) are in the slope region (Table 1). The shelfbreak follows the northern margin of the Ewing Bank, Mississippi Canyon, and southern Viosca Knoll areas (blue line, Figure 1).
The CO2 storage reservoir screening system and the CO2 storage potential assessment employed in this study focused on the slope area, and the sands are distributed at the south and southeast of the shelf–slope boundary in Ewing Bank, Mississippi Canyon, Southern Viosca Knoll, Green Canyon, Atwater Valley, and Walker Ridge protraction areas (Table 2). The slope region fields in the eastern portion of the study area (i.e., Southern Viosca Knoll and Mississippi Canyon protraction areas) were prioritized in storage estimation (Section 4.4) due to their proximity to the shoreline and the associated infrastructure. These fields require offshore transportation infrastructure for the development of CO2 storage and CO2-EOR sites.
Previous studies revealed that saline formations and hydrocarbon reservoirs in the study area were strongly affected by salt tectonics. On the Louisiana Shelf, reservoir strata were deposited above allochthonous salt that accumulated above an Oligocene–Miocene detachment. Strata are complexly faulted and dominated by Roho structures and associated diapiric salt bodies [19,20]. The upper continental slope contains a variety of allochthonous salt bodies developed above a system of ramps and flats that rise southward from the Mesozoic section into the Pleistocene–recent section. This area contains numerous allochthonous salt bodies and turbidite mini-basins with reservoirs distributed throughout the mini-basins [21,22,23,24]. Reservoirs consist of turbidite channel-fan deposits, and reservoir sands include a complex mosaic of channel, levee, proximal fan, and distal fan deposits [25,26,27].

3. Methodology

3.1. Dataset

The data used in this assessment are primarily from the Bureau of Ocean Energy Management’s (BOEM) 2018 Sands Atlas (https://www.data.boem.gov/Main/GandG.aspx) (accessed on 2 September 2021) and include detailed information on individual wells and their productive sands in the central GOM. Sand names in the BOEM database are unique and associated with a play number and field name. Thus, each sand is essentially the individual reservoir in each field. Production data for each sand are provided in the database, assuming that the sands are not in communication with each other. Therefore, structures and reservoir properties are also assumed to be distinct for each sand and should reflect distinct storage resources for each reservoir. The ranges of values for some of the parameters obtained from the BOEM database for the sands from our study area are listed in Table 3. The important sand attributes available for each sand body include sand location, subsea depth, water depth, sand thickness, initial temperature, initial pressure, porosity, permeability, water saturation, and hydrocarbon production information (e.g., original oil in place, original gas in place, original barrel of oil equivalent (BOE), etc.).

3.2. CO2 Density Estimation

An accurate estimation of CO2 density is required to understand the state of CO2 in the reservoir condition and choose the storage sites that will allow the injected CO2 to be stored in the reservoir in the supercritical state. CO2 density is also an important parameter to estimate storage resources using the correlation developed by NETL [16]. In this study, CO2 density was estimated at the initial reservoir conditions using the prediction method developed by Bikkina et al. [17] and compared (Figure 2) with the predictions from the National Institute of Standards and Technology (NIST) database [28,29]. The temperature and pressure ranges of the prediction method from Bikkina et al. [17] are 53.5 °F (12 °C) to 212 °F (100 °C) and 1 to 600 bars, respectively. In general, the predictions from Bikkina et al. [17] were very similar to the NIST predictions, even for the temperature and pressure values that exceed the limit of the method (Figure 2). The mean absolute error (MAE) between the two methods was 0.013 g/cm3, and the root mean square deviation (RMSD) was 0.015 g/cm3. It should also be mentioned that the NIST methodology is applicable to the density of pure CO2, whereas Bikkina et al. [17] assumed the CO2 to be saturated with water, which offers a better approximation of the state of CO2 after injection into the reservoir. Hence, the densities estimated by Bikkina et al. [17] were used in this study for site screening and storage estimation, discussed in Section 3.3 and Section 3.4.

3.3. CO2 Storage Sites Screening Criteria

In this study, the reservoir screening criteria of Raza et al. [30], developed for depleted gas reservoirs, and Smith et al. [15], primarily defined for CO2-EOR, were combined with the screening criteria proposed for the study area using the analysis of the geologic attributes (temperature, pressure, porosity, permeability, and API gravity) and the published geologic studies in the region [4,22,23,31,32].
The main aspects considered for screening CO2 storage sites were storage capacity, injectivity, trapping mechanism, and containment. Reservoir temperature, pressure, and CO2 density play big roles in determining the storage capacity of the reservoirs. Denser supercritical CO2 occupies a smaller pore volume, allowing maximum pore volume utilization and mobility across the reservoir. The density of CO2 increases with depth, which is why many studies have reported that efficient storage takes place in sites that are at least 800 m deep [33,34,35,36,37,38]. The porosity of the reservoir, which decreases with depth, should also be high enough to ensure maximum storage capacity. There are other aspects, such as the geometry of depositional facies, the buoyancy of CO2, and irreducible water saturation, that can also affect the efficiency of storage capacity [37,39,40]. However, these factors were not considered in this study due to a lack of data.
The injectivity of reservoirs depends on how well the injected fluid can flow through the stratigraphic intervals. This aspect is mainly controlled by the reservoir pressure, permeability, and thickness. Low permeability and thin reservoir intervals adversely affect the CO2 injectivity. Studies have revealed that reservoirs with high (>100 mD) near wellbore permeability require a lesser number of injection wells for favorable injection [41]. Increased reservoir pressure with CO2 injection can also limit the injectivity and storage capacity due to excessive pressure buildup, especially for reservoirs with natural water drive [42,43]. Bachu [44] reported a 3% decrease in storage capacity in oil and gas reservoirs supported by weak water drive. Other factors that can affect CO2 injectivity in oil and gas reservoirs but were not considered in this study include mineral dissolution or precipitations due to geochemical reactions between rocks and fluids.
Screening the reservoirs on the aspects of trapping mechanism is very tricky because, depending on the type of trapping, a lot of physico-chemical and geological properties such as reservoir temperature, pressure, CO2–Brine/H2O interfacial tension, rock wettability, capillary pressure, viscosity, geometry of pores, etc., may impact storage [14,45,46,47,48]. In the scope of this study and keeping the availability of data in mind, only reservoir temperature, pressure, and rock type were considered for screening. Reservoir pressure and temperature affect the density of CO2 and the rate at which CO2 plumes migrate upward [49]. Reservoir conditions also affect the dissolution of CO2 into the formation fluid. CO2 solubility in formation fluid increases with pressure and decreases with temperature and salinity of formation water [50].
Seal geometry (lateral continuity and thickness) and hydraulic integrity of the reservoirs are the key aspects of storage site containment [39]. Hydrocarbon accumulation without associated seeps in the studied sands indicates seal integrity of the caprocks in the reservoirs. However, seal integrity might change due to the increase in pore pressure upon CO2 injection. A significant increase in the pore pressure might cause mechanical breakdown of the seals [51,52]. Therefore, the hydraulic integrity of the reservoir must also be considered during site screening. Reservoirs that are normally pressured to weakly over-pressured are optimal for CO2 storage. The integrity of the seal also depends on its thickness. Different studies have suggested different cut-off numbers for seal thickness. Ramírez et al. [53] suggested that seals should have at least 10 m of thickness to prevent cross-formational flow of CO2, whereas Raza et al. [30] proposed 100 m as the minimum seal thickness for depleted gas reservoirs. Published geological studies in the central GOM region indicate numerous shale intervals in the Miocene–Pleistocene section between 50 and 100 m thick [4,22,23,31,32]. Many normal faults exist within the slope minibasins, and these faults pose the greatest risk for cross-formational flow, particularly where original reservoir pressure approaches fracture pressure. Indeed, joints are largely absent in Gulf of Mexico mudrocks, and documented seeps are commonly along faults and salt margins [54].

3.4. CO2 Storage Estimation Methods

The primary method used for CO2 storage estimation is the method provided by the U.S. Department of Energy’s National Energy Technology Laboratory [16], referred to as the NETL method in this study. The CO2 storage efficiency factor (Eoil/gas) was chosen as 15%, 25%, and 40% for low (P10), medium (P50), and high (P90) resource estimations, respectively. These efficiency factor values were considered based on the fact that the sands in continental slope areas tend to be more homogenous, and the experience from water flooding shows that recovery could approach 40% in some of the fields [55]. The equation is provided below:
G C O 2 = A h n φ e   ( 1 S w i ) B ρ C O 2 E o i l / g a s ,  
where
G C O 2 = mass estimate of oil and gas reservoir CO2 storage resource, unit *: M;
A = area that defines the oil or gas reservoir that is being assessed for CO2 storage, unit *: L2;
hn = net oil and gas column height in the reservoir, unit *: L;
φe = average effective porosity **;
Swi = average initial water saturation within the reservoir unit *: L3/L3;
B = fluid formation volume factor, unit *: L3/L3;
ρ C O 2 = density of CO2 evaluated at reservoir pressure and temperature, unit *: M/L3;
Eoil/gas = CO2 storage efficiency factor, the volume of CO2 stored in an oil or gas reservoir per unit volume of original oil or gas in place (OOIP or OGIP), unit *: L3/L3;
* L = length; M = mass.
** The studied sands have good permeability, so the average effective porosities are assumed to be equal to the average porosities of the sands.
In addition, the volumetric method [15] was also used to estimate CO2 storage resources and then compared with those calculated using the NETL method [16]. Generally, the volumetric method estimates the theoretical maximum storage resource of the reservoir. It should also be noted that these storage estimation methods are static and do not differentiate between different trapping potentials. Mechanisms such as the dissolution of CO2 into brines [56] or crude oil and mineralization [57] can increase the estimated storage resource, which was not considered in this study. An integrated reservoir model coupled with wellbore and reservoir properties would provide a more robust estimation of CO2 storage resources and reservoir behavior within the fields as well as help understand other dynamics of CO2 storage, such as trapping mechanisms, injectivity, and plume migration [58]. The following are the CO2 storage resource estimation functions from Smith et al. [15] for the volumetric method:
Q = A T φ ρ CO 2   ( 1 S w ) ,
where
Q = storage resource of the oil reservoir, tonne (metric) CO2;
A = field area, m2;
T = producing interval thickness, m;
φ = average reservoir porosity, %;
ρ CO 2 = density of CO2, g/cc;
1 − Sw = saturation of oil, where Sw is the initial reservoir water saturation, %.

4. Results and Discussion

4.1. Key Screening Criteria Comparison between Shelf and Upper Slope

4.1.1. Reservoir Temperature and Pressure

One of the critical screening criteria in the identification of suitable CO2 storage reservoirs is the reservoir temperature. In general, the temperature vs. subsea depth plot of the slope (Figure 3) area shows a relatively strong positive 0.67 Pearson correlation between the two parameters, impacted by the cooling effect of the water column over a broad range of seabed depth (718 m to 9388 m), as well as thermal effects associated with salt bodies.
To better understand the initial temperature distribution of the slope sands, the initial temperature and the subsea depth of the sand by the well location were examined (Figure 4). The initial temperatures of the slope sands ranged from 22.8 °C (73 °F) to 164.4 °C (328 °F), while sand subsea depths ranged from 718 m (2355 ft) to 9388 m (30,800 ft). As illustrated by the initial temperature vs. subsea depth correlation plot (Figure 3), low-temperature sands generally correspond with lesser subsea depth, while high-temperature sands generally correspond with greater subsea depths (larger bubble size). Broadly, the spatial distribution of sands shows that a cluster of higher temperature sands is located near the northwest and north margin of the Mississippi Canyon and southern Viosca Knoll protraction areas, as well as associated with some deep wells in the Mississippi Canyon, Green Canyon, Ewing Bank, and Walker Ridge protraction areas (Figure 4).
The sand temperature gradient map (Figure 5) shows a gradual decrease in the temperature gradient from the shelf–slope boundary down to the slope area except in the Walker Ridge (WR) area, where the temperature gradient slightly increased compared to the temperature gradients of the sands in the Green Canyon (GC) and Atwater Valley (AT) protraction areas.
In addition to reservoir temperature, reservoir pressure is also critical for the identification of suitable CO2 storage sites. Figure 6 shows a strong and statistically significant Pearson correlation between initial pressure and subsea depth for the slope area. The observations are below the lithostatic gradient of 22.6 KPa/m (1.0 psi/foot) but mostly higher than the hydrostatic gradient of 9.8 KPa/m (0.433 psi/ft) in the slope area based on the initial reservoir temperature and pressure conditions. Reservoirs below lithostatic pressure gradient have a high potential for storage because there is considerable headroom for injection without stressing the reservoir. The headroom for injection increases as the pressure depletes with the production of hydrocarbons.
Maximum initial reservoir pressure reaches 148,989 kPa in the slope area. The spatial distribution of initial pressure and subsea reservoir depth (Figure 7) also reveals a positive correlation between the initial reservoir pressure and subsea depth. High-pressure sands (yellow and orange colors, 72,010–148,989 kPa) are located in the southern and southeast of the slope area. The initial pressure of sands close to the shelf–slope boundaries is relatively low (dark color, 8094–33,116 kPa).
The pressure–depth quotient map (Figure 8) shows the pressure–depth gradient of each sand. Here, the yellow and green colors indicate that the sands have initial pressure–depth quotients (15.5–19.3 kPa/m) close to the lithostatic gradient and thus little headroom for CO2 injection prior to hydrocarbon production. These high-pressure–depth quotient sands are scattered throughout the region. The dark purple color indicates that reservoirs with relatively low initial pressure–depth quotients (9.5–12.2 kPa/m) are distributed especially at the northwest corner and north margin of Mississippi Canyon, and few sands are at the east margin of the south Viosca Knoll, indicating significant headroom for injection. The headroom is even higher in reservoirs that have been depressurized by hydrocarbon production.
From the initial temperature and initial pressure spatial distribution map of the sands in the slope area (Figure 9), it is observed that northern boundary sands generally have high initial temperatures with relatively low pressures (pink, light pink, and purple colors). Conversely, a number of sands located in the Green Canyon, Walker Ridge, and Mississippi Canyon areas are in high initial pressure conditions with correspondingly high initial temperatures (deep blue color).
However, when interpreting our findings, it is important to keep in mind that the initial temperature and pressure values utilized in our study to characterize the storage sites may not be reflective of the conditions in the mature reservoir state. Pressure depletion is an issue, although the shut-in pressure tests indicate rapid pressure rebound. Cooling of mature reservoirs by fluid flow and adiabatic gas expansion is probably a factor, but no data on mature reservoir temperature were found. Accordingly, original pressures and temperatures appear adequate for assessment, but pressure decline/recovery characteristics and mature reservoir temperature should be considered when considering pilot programs and injection design.

4.1.2. Reservoir Porosity and Permeability

Porosity and permeability influence the total volume of CO2 that can be stored and the rate at which CO2 can be injected into a given reservoir. For data from slope areas, porosity and permeability semi-log scale plots show a positive and statistically significant linear relationship (Figure 10). Porosity values appear to cluster between 20% and 35%, while permeability values are commonly greater than 100 mD. It is important to note that Darcy-class permeability was also observed in the slope area, so reservoir properties are regionally favorable for CO2 storage.
In addition, the porosity–permeability distribution map (Figure 11) shows that most of the sands are in favorable porosity and permeability range (deep blue color, >20% porosity and >100 mD permeability). Some sands with good porosity but low permeability are also scattered in the slope region (pink color, >20% porosity and <100 mD permeability). Only a few sands have unfavorable porosity and permeability conditions for CO2 storage in the slope area (white color, <20% porosity and <100 mD permeability).

4.1.3. Gas–Oil Ratio and API Oil Gravity

Plotting the gas–oil ratio vs. API gravity in slope reservoirs in the SECARB offshore area (Figure 12) reveals that most reservoirs have gas–oil ratios between 0.4 and 10. Where the gas–oil ratio exceeds 100, oil gravity is commonly not reported. In general, a low gas–oil ratio favors the sweep of hydrocarbons by injection of CO2. Miscible CO2 flooding is possible where API gravity is between 22° and 48°, but values between 30° and 40° are commonly considered optimal [59].

4.2. Screening Criteria

After studying the data and combining the screening criteria from Raza et al. [53] and Smith et al. [15], a total of 10 screening criteria were proposed and applied to screen sands in this study (Table 4). These factors reflect the storage capacity, injectivity, solubility trapping, capillary trapping, and containment aspects of CO2 storage sites.
Due to the scope of the study, other CO2 storage screening criteria, including lateral continuity of the seal, thickness of the seal, and secondary recovery phase of the reservoir, were not applied.

4.3. CO2 Storage Site Screening Platform

The SAS® Viya Explore and Visualization interface provides excellent functionality for building the CO2 storage screening platform. A total of 6537 observations (the unique sand bodies in each BOEM field) from the shelf area and 956 observations from the slope area were mapped in SAS® Viya. The filter function provides easy handling of the observations based on the attributes. The range of the value distribution for each variable appears along the number axis of that filter, and the user can filter the values in real-time using slider bars. Several important screening criteria are included in the reservoir screening platform in SAS® Viya (Figure 13, right-hand portion). In addition to the filter function, users can specify the color and size of the marker and label attributes to visualize the observations.
The SAS® Viya platform is highly interactive and enables visualization of the data through the map view. Additionally, filters can be adjusted to display screening criteria in real-time. Users may quickly change the criterion ranges to fit a given purpose with a series of sliders. Figure 14 shows the distribution of the sands in the slope area (956 sands).
For the 956 sands in the slope area, the counts of filtered sands are listed in Table 5 with the corresponding screening criteria. Over 308 sands were filtered out in order to meet the API gravity range between 22°–48°. In addition, 212 sands were filtered due to less than 10,000 barrels of cumulative production, and 186 sands were filtered out because of less than 100 mD permeability. After applying all screening criteria, the original 956 sands were filtered down to 445 sands in the slope area. Most of the filtered sands are found in the Mississippi Canyon, Green Canyon, and Viosca Knoll areas. The CO2 storage site screening criteria filters and corresponding ranges are displayed in Figure 15.

4.4. CO2 Storage Estimation

After applying the screening criteria established in Table 1 to the sands in the slope area, the CO2 storage estimations were recalculated following the NETL method. The estimated storage capacity (NETL P50) of the screened BOEM fields in the slope area is 1.05 gigatons in total (445 satisfied sands in Table 5).
Table 6 shows the top 10 CO2-estimated storage BOEM fields. MC807 is the highest CO2 storage target, with an estimated 68% more storage resources than the second-ranked field (GC743). A total of four fields in the slope area have an estimated P50 storage capacity greater than 50 Mt.
As discussed in Section 2, close proximity to the Mississippi Delta may allow for the less costly development of fields located in the Mississippi Canyon and Viosca Knoll protraction areas. Table 7 provides an account of the estimated CO2 storage resources for the top 10 fields from these two protraction areas, and Figure 16 shows the location of the top 10 fields in the Mississippi Canyon and Visco Knoll protraction areas.
Among the 10 fields, MC807 is the highest-ranked field with over 150 Mt storage resources based on the NETL P50 estimation method. The remaining fields in these two protraction areas have an estimated NETL P50 storage resource of less than 50 Mt. The corresponding reservoir sizes and geological conditions for these fields are provided in Table 8 and Table 9, respectively.
One explanation for the high estimated storage resource of the MC807 block is the advanced field development (26 sand bodies across most of the block) in this block (Table 8). The other high-ranking blocks in the Mississippi Canyon and Viosca Knoll areas completed fewer than 10 producing sand bodies, and the well patterns are much more localized than in MC807. Importantly, many of the field areas estimated by BOEM are based on the current state of development rather than the overall size of the oil accumulation, and refined estimates of potential productive areas are being delineated seismically and may result in a significant expansion of the storage resource.
To further rank the CO2 storage resource, the CO2 storage resource per unit area was calculated using SAS® Viya. Here, the estimated CO2 storage resource for each sand was divided by the productive area specified by BOEM, and the data were aggregated at the field level. Table 10 lists the top-ranked fields in the Mississippi Canyon and Viosca Knoll areas based on storage resource (NETL P50 estimation method) per unit area (km2). Notably, the 10 highest-ranked fields are all from the Mississippi Canyon protraction area and the MC776 field has the highest storage resource per unit area (estimated P50 = 1.48 Mt/km2). Table 11 provides an overview of the reservoir conditions for each of these fields.
It should be noted that this study aimed to provide a high-level static assessment of the suitability of the studied sands for CO2 storage. The estimated storage resources are theoretical maximum and do not take different trapping mechanisms, plume geometry, and plume dynamics into consideration, which may affect the storage potential. For example, the dissolution of injected CO2 into the formation fluid can increase the storage resource estimated with NETL or volumetric methods. The dynamics of CO2 at subsurface conditions can also alter this estimated storage resource. For example, if the buoyancy force exerted by the formation fluid is higher than the sealing capillary pressure, the injected CO2 can migrate to the seal rock and eventually escape from the storage site, affecting the storage potential. Hence, to further assess the storage capacity of the sands, a detailed investigation of different types of trapping potentials of the sands and how the injected CO2 would behave in the subsurface formation in the presence of other fluids should be considered in future studies.
An opportunity exists to prolong the life of the oil fields in the continental slope through CO2-enhanced oil recovery with associated storage, and the success of waterflooding operations in increasing recovery and growing reserves is promising for the technology. Several logistical factors need to be considered, and careful thought and reservoir modeling efforts are required to design a system of injection and production wells, determine optimal well spacing, and organize well patterns to minimize the risk of cross-formational flow along faults. For example, aligning producers between injectors and faults will help minimize the risk of pressure buildup and flow of CO2 into fault systems. Obtaining CO2 supply is another challenge, and pipelines and shipping appear to be the most viable options. Limited platform space is a factor that challenges the implementation of waterflood operations [11], and so the same hurdle challenges the implementation of CO2-enhanced recovery operations. Other challenges include installing corrosion-resistant tubing strings in wells that are CO2-ready and installing recycle loops for reinjection of CO2 that is co-produced with the oil. Meeting these challenges will prolong the life of deepwater fields while contributing substantially to greenhouse gas reduction goals in the region.

5. Conclusions

In this study, the SAS® Viya platform was utilized to manage geological datasets and analyze the geological characteristics of the sands in shelf and slope areas through the use of correlation plots and sand feature distribution maps. In the slope area, the pressure and temperature show a linear positive correlation to depth. The porosity vs. permeability plot shows the sands in the slope area typically have 20–35% porosity and permeability greater than 100 mD, which indicates favorable objectives for CO2 injection. Most of the sands in the continental slope have a gas–oil ratio of less than 10 Mcf/bbl and 22°–48° API gravity that is favorable for CO2-EOR.
A series of screening criteria to characterize the hydrocarbon reservoirs and analyze their CO2 storage and EOR potential were defined. Reservoir properties, fluid properties, and production history were considered in the design of the system. Ten screening criteria were employed. The SAS® Viya platform was used to filter data from 956 sand bodies in the slope area. The screening procedure identified 445 reservoirs prospective for CO2 injection in the existing fields, which are mainly in the Green Canyon, Mississippi Canyon, and Viosca Knoll protraction areas.
Storage estimation revealed that at a regional level, after applying the screening criteria, 1.05 gigatons of CO2 storage resources (NETL P50 estimation method) are available in the developed reservoirs in the continental slope area. The fields with the largest overall projected CO2 storage resource were found in the Mississippi Canyon protraction area. Therefore, near-term development initiatives may seek to focus efforts in the Mississippi Canyon area because of its close proximity to the Mississippi Delta and large estimated CO2 storage resources. Even though the Green Canyon has fields with high geologic storage potential (Table 3 and Table 4), it is not a good candidate for CO2 storage; the shelf is highly faulted, which limits reservoir size, and the Green Canyon lies offshore across the shelf and thus requires installation of infrastructures like pipelines to reach.
Due to their proximity to the Delta, the Mississippi Canyon and Viosca Knoll protraction areas were examined in more detail. For these two protraction areas, the top ten fields had an estimated CO2 storage resource of 363 Mt (NETL P50 estimation method). Importantly, of the fields analyzed in the Mississippi Canyon and Viosca Knoll protraction areas, the top ten most prospective fields (based on P50 estimations storage per unit area) are located in the Mississippi Canyon area. This observation suggests that future developmental activities may benefit from focusing efforts in the Mississippi Canyon area.
It is also noteworthy that the considerable amount of storage resources in the Mississippi Canyon makes it “low-hanging fruit” for near-term CO2 storage, given the in-place platform infrastructure and, potentially, usable pipelines. However, expansion into non-hydrocarbon bearing reservoirs (i.e., saline reservoirs) proximal to the oil accumulations is a logical next step. Hence, using traditional geological workflows coupled with data mining, future studies can evaluate storage resources beyond/below the oil–water contact.

Author Contributions

Conceptualization, X.H., J.C.P. and P.B.; methodology, X.H., R.B., J.C.P. and P.B.; software, X.H., R.B., K.B. and G.C.; validation, X.H., R.B., G.C., J.C.P. and P.B.; formal analysis, X.H., R.B., K.B., J.C.P. and P.B.; investigation, X.H., R.B., K.B., J.C.P. and P.B.; resources, G.C., J.C.P. and P.B.; data curation, X.H.; writing—X.H. and R.B.; writing—review and editing, X.H., R.B., P.B. and J.C.P.; visualization, X.H. and R.B.; supervision, G.C., J.C.P. and P.B.; project administration, G.C., J.C.P. and P.B.; funding acquisition, G.C., J.C.P. and P.B. All authors have read and agreed to the published version of the manuscript.

Funding

The National Energy Technology Laboratory (NETL) of the United States Department of Energy (DOE) provided funding (Award No. DE-FE0031557) for this study through the Southern States Energy Board. Cost share support for this research was supplied by the project partners, including the SAS Institute. This paper is based upon work supported by the Department of Energy and was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendations, or favoring by the United States Government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof.

Data Availability Statement

Publicly available datasets were analyzed in this study. This data can be found here: https://www.data.boem.gov/Main/GandG.aspx (accessed on 2 September 2021).

Conflicts of Interest

The authors declare no conflicts of interest.

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Figure 1. Well location map of the SECARB offshore area. Wells were classified into shelf area and slope area by shelf–slope boundary (dark blue line). Sand body information is from the Bureau of Ocean and Energy Management’s 2018 Sands Atlas (https://www.data.boem.gov/Main/GandG.aspx (accessed on 2 September 2021)).
Figure 1. Well location map of the SECARB offshore area. Wells were classified into shelf area and slope area by shelf–slope boundary (dark blue line). Sand body information is from the Bureau of Ocean and Energy Management’s 2018 Sands Atlas (https://www.data.boem.gov/Main/GandG.aspx (accessed on 2 September 2021)).
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Figure 2. CO2 density prediction by Bikkina et al. [17] vs. NIST method. Blue markers represent the CO2 prediction of the sands within the Bikkina et al. [17] pressure and temperature model prediction range, and grey color markers are the CO2 density predictions that exceed the Bikkina et al. [17] model prediction range.
Figure 2. CO2 density prediction by Bikkina et al. [17] vs. NIST method. Blue markers represent the CO2 prediction of the sands within the Bikkina et al. [17] pressure and temperature model prediction range, and grey color markers are the CO2 density predictions that exceed the Bikkina et al. [17] model prediction range.
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Figure 3. Initial temperature vs. subsea depth in the slope area.
Figure 3. Initial temperature vs. subsea depth in the slope area.
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Figure 4. Initial temperature and subsea depth of the sands in the slope zone. Note that color shade corresponds to initial temperature while symbol size corresponds to subsea depth (m).
Figure 4. Initial temperature and subsea depth of the sands in the slope zone. Note that color shade corresponds to initial temperature while symbol size corresponds to subsea depth (m).
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Figure 5. The temperature gradient and subsea depth of the sands in the slope zone. The general temperature gradient shows a decreasing trend from the shelf–slope boundary to the slope Green Canyon (GC) and Atwater Valley (AT) area.
Figure 5. The temperature gradient and subsea depth of the sands in the slope zone. The general temperature gradient shows a decreasing trend from the shelf–slope boundary to the slope Green Canyon (GC) and Atwater Valley (AT) area.
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Figure 6. Initial reservoir pressure vs. subsea depth in the slope area.
Figure 6. Initial reservoir pressure vs. subsea depth in the slope area.
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Figure 7. The initial pressure and subsea depth of the slope sands.
Figure 7. The initial pressure and subsea depth of the slope sands.
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Figure 8. The pressure–depth quotient map of the slope sands. Dark purple color represents low-pressure–depth gradient sands and the yellow color indicates the sands that are close to the lithostatic gradient. It is important to note that sands near the hydrostatic gradient have significant headroom for CO2 injection.
Figure 8. The pressure–depth quotient map of the slope sands. Dark purple color represents low-pressure–depth gradient sands and the yellow color indicates the sands that are close to the lithostatic gradient. It is important to note that sands near the hydrostatic gradient have significant headroom for CO2 injection.
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Figure 9. The initial pressure and initial temperature of the sands in the slope zone. Bubble size indicates sand depth, and bubble color indicates the relative initial pressure and relative initial temperature. Low temperature to medium temperature boundary is 64.4 °C, and medium temperature to high temperature boundary is 86.1 °C. Low pressure to medium pressure boundary is 43,154 kPa, and medium pressure to high pressure boundary is 64,390 kPa.
Figure 9. The initial pressure and initial temperature of the sands in the slope zone. Bubble size indicates sand depth, and bubble color indicates the relative initial pressure and relative initial temperature. Low temperature to medium temperature boundary is 64.4 °C, and medium temperature to high temperature boundary is 86.1 °C. Low pressure to medium pressure boundary is 43,154 kPa, and medium pressure to high pressure boundary is 64,390 kPa.
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Figure 10. Porosity vs. permeability (log scale) for sands located in the slope area.
Figure 10. Porosity vs. permeability (log scale) for sands located in the slope area.
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Figure 11. Porosity and permeability of the sands in the slope area. Overall, 20% is the low and high boundary of the porosity, and 100 mD is the low–high boundary of permeability. Most of the sands in the slope area are within the high porosity and high permeability boundary (dark blue color), which is favorable for CO2 storage.
Figure 11. Porosity and permeability of the sands in the slope area. Overall, 20% is the low and high boundary of the porosity, and 100 mD is the low–high boundary of permeability. Most of the sands in the slope area are within the high porosity and high permeability boundary (dark blue color), which is favorable for CO2 storage.
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Figure 12. Plot of gas–oil ratio (log scale) versus API gravity for oil-rich slope reservoirs in the SECARB offshore project area.
Figure 12. Plot of gas–oil ratio (log scale) versus API gravity for oil-rich slope reservoirs in the SECARB offshore project area.
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Figure 13. SECARB offshore CO2 storage screening platform. Blue color and red color represent the subsea depth of the sand, and symbol size corresponds to original oil in place (OOIP).
Figure 13. SECARB offshore CO2 storage screening platform. Blue color and red color represent the subsea depth of the sand, and symbol size corresponds to original oil in place (OOIP).
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Figure 14. Distribution of sands in the slope color-coded by subsea depth. Size correlates to original oil in place (OOIP).
Figure 14. Distribution of sands in the slope color-coded by subsea depth. Size correlates to original oil in place (OOIP).
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Figure 15. The remaining 445 slope sands after applying the screening criteria defined in Table 4 of this study.
Figure 15. The remaining 445 slope sands after applying the screening criteria defined in Table 4 of this study.
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Figure 16. The top ten BOEM fields in terms of estimated CO2 storage resources are from Mississippian Canyon and Viosca Knoll protraction areas.
Figure 16. The top ten BOEM fields in terms of estimated CO2 storage resources are from Mississippian Canyon and Viosca Knoll protraction areas.
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Table 1. Number of depleted and active fields/reservoir sands in the central GOM.
Table 1. Number of depleted and active fields/reservoir sands in the central GOM.
RegionField StatusFieldsSands
ShelfActive2074940
Depleted3021597
Total5096537
SlopeActive114838
Depleted50118
Total163956
Grand Total6727493
Table 2. Protraction areas and number of fields/sands in the upper slope region of the study area.
Table 2. Protraction areas and number of fields/sands in the upper slope region of the study area.
Protraction AreasStatusFieldsSands
Atwater Valley ATActive29
Depleted45
Ewing Bank EWActive13138
Depleted510
Green CanyonActive34253
Depleted1331
Mississippi Canyon MCActive44340
Depleted1953
Viosca Knoll VKActive1476
Depleted919
Walker Ridge WRActive722
Grand Total164956
Table 3. Reservoir properties from the BOEM database for our study area.
Table 3. Reservoir properties from the BOEM database for our study area.
ShelfSlope
Sand Counts6537956
Average Subsea Depth (feet)8971.12 (2734.40 m)13,100.97 (3993.18 m)
Average Thickness (feet)21.75 (6.63 m)38.29 (11.67 m)
Average Area (acres)581.29 (2.35 km2)901.33 (3.65 km2)
Average Temperature (°F)183.49 (84.16 °C)169.17 (76.21 °C)
Average Pressure (psi)5056.42 (34.86 mPa)8599.45 (40.68 mPa)
Average Porosity 0.280.29
Average Permeability (mD)391.03589.56
Average Water Saturation0.280.25
Average Original Barrel of Oil Equivalent (BOE) (bbl)3,895,682.04
(619.36 million L)
14,682,604.78
(2334.35 million L)
Table 4. Screening criteria applied in this study.
Table 4. Screening criteria applied in this study.
ParametersPositive IndicatorsIndication Aspect
Subsea Depth≥2304 feet (702 m)Storage Capacity
Porosity≥20%Storage Capacity Capillary Trapping
Permeability≥100 mDInjectivity
Initial Reservoir Temperature>CO2 critical temperature (304.13 K, 31.0 °C, 87.8 °F)Storage Efficiency
Pressure>CO2 critical pressure (7.3773 MPa, 72.8 atm, 1070 psi, 73.8 bar)Storage Efficiency
Pressure–Depth Quotients<15.5 KPa/m (0.68 psi/ft)Injectivity
API Gravity22°–48° feasible (medium-light crude oil); 30°–40° considered optimal (light crude oil) [59]Injectivity
Cumulative Production≥10,000 barrels (1.59 million L)Storage Potential
Rock TypeQuartz-rich sandstone, typically poorly consolidatedCapillary Trapping
CO2 Density>0.6 g/ccStorage Capacity
Table 5. The counts of satisfied sands and filtered sands in the slope area with corresponding screening criteria.
Table 5. The counts of satisfied sands and filtered sands in the slope area with corresponding screening criteria.
Screening CriteriaSatisfied SandsFiltered Sands
Cumulative Oil (≥1.59 million L, 10,000 bbl)744212
Initial Temperature (≥31.1 °C, 87.98 °F)94214
Initial Pressure (≥7.3773 MPa, 1070 psi)9560
Subsea Depth (≥702 m, 2304 feet)9560
CO2 Density (>0.6 g/cc)9551
Permeability (≥100 mD)770186
Porosity (≥20%)91937
Oil API Gravity (22°–48°, API units)648308
All Conditions445511
Table 6. The top ten BOEM fields from slope area in terms of estimated CO2 storage resources.
Table 6. The top ten BOEM fields from slope area in terms of estimated CO2 storage resources.
BOEM FieldNETL Method—Low
(P10), Eoil/Gas = 15%
(Megatons)
NETL Method—Medium
(P50), Eoil/Gas = 25%
(Megatons)
NETL Method—High
(P90), Eoil/Gas = 40%
(Megatons)
Volumetric Method
Storage Resource
(Megatons)
MC8071081812891052
GC74364107171543
GC8265998158451
GC6405388141456
GC654294877221
MC776223759206
MC778172845154
MC084172844151
GC562132134117
MC69610172790
Table 7. The top ten BOEM fields in terms of estimated CO2 storage resources are from Mississippian Canyon and Viosca Knoll protraction areas.
Table 7. The top ten BOEM fields in terms of estimated CO2 storage resources are from Mississippian Canyon and Viosca Knoll protraction areas.
BOEM FieldNETL Method—Low
(P10), Eoil/Gas = 15%
(Megatons)
NETL Method—Medium
(P50), Eoil/Gas = 25%
(Megatons)
NETL Method—High
(P90), Eoil/Gas = 40%
(Megatons)
Volumetric Method
Storage Resource
(Megatons)
MC807 108 181 289 1052
MC776 22 37 59 206
MC778 17 28 45 154
MC084 17 28 44 151
MC696 10 17 27 90
MC194 10 16 25 112
VK956 10 16 25 142
MC935 8 14 22 71
VK990 8 13 21 80
MC383 8 13 20 75
Table 8. The reservoir sizes of the top ten BOEM fields from Table 7.
Table 8. The reservoir sizes of the top ten BOEM fields from Table 7.
BOEM
Field
Count of
Sands
NETL Medium Storage
Resource (P50) (Megatons)
Total Area
(km2)
Average Area
(km2)
Average Reservoir
Thickness (m)
Average Subsea
Depth (m)
MC807 26 181 325.5917.3416.475144
MC776 4 37 25.078.6934.716047
MC778 7 28 48.309.5517.746822
MC084 6 28 51.8811.9919.854028
MC696 4 17 24.898.6215.067003
MC194 8 16 65.2911.316.812622
VK956 4 16 85.0329.477.803783
MC935 3 14 18.298.4422.535272
VK990 8 13 36.756.357.692331
MC383 2 13 22.7415.7611.583812
Table 9. The geological conditions of the top ten BOEM fields from Table 7.
Table 9. The geological conditions of the top ten BOEM fields from Table 7.
BOEM
Field
Average Initial
Reservoir
Pressure (MPa)
Average Initial
Reservoir
Temperature (°C)
Average
Permeability
(mD)
Average
Porosity
Average
Water
Saturation
Total OOIP
(Billion L)
Total ROIP
(Billion L)
MC807 80.7176.28491.12 0.29 0.20 148.257.20
MC776 92.3992.641062.50 0.27 0.16 54.801.45
MC778 107.90115.39653.71 0.23 0.15 68.632.01
MC084 50.4275.65511.00 0.27 0.20 114.3811.60
MC696 104.79111.25902.25 0.25 0.18 706.6867.82
MC194 32.7159.93497.13 0.32 0.29 52.671.39
VK956 49.1699.44688.25 0.29 0.19 124.716.62
MC935 86.0373.33441.67 0.27 0.22 58.160.01
VK990 31.3656.74422.38 0.31 0.29 49.270.91
MC383 54.7763.062266.00 0.34 0.18 49.642.03
Table 10. The top ten BOEM fields in terms of storage resources per unit area from Mississippi Canyon and Viosca Knoll and corresponding reservoir size.
Table 10. The top ten BOEM fields in terms of storage resources per unit area from Mississippi Canyon and Viosca Knoll and corresponding reservoir size.
BOEM
Field
Count of
Sands
NETL Medium (P50)
Storage Resource per Unit
Area (Megatons/km2)
Total
Area (km2)
Average
Area (km2)
Average Reservoir
Thickness (m)
Average Subsea
Depth (m)
MC77641.48 25.076.2734.716047
MC02911.320.450.4528.912932
MC89930.939.913.3022.864951
MC69810.903.533.5220.644886
MC93530.7718.306.1022.535272
MC69640.6824.896.2215.087002
MC80010.630.700.7017.814833
MC68210.6112.8612.8626.057520
MC77870.5948.306.9017.746821
MC807260.55325.5912.5216.475144
Table 11. Geological characteristics of the top ten BOEM fields from Table 10.
Table 11. Geological characteristics of the top ten BOEM fields from Table 10.
BOEM
Field
Reservoir
Pressure (MPa)
Reservoir
Temperature (°C)
Permeability
(mD)
Porosity Water
Saturation
Total OOIP
(Billion L)
Total ROIP
(Billion L)
MC776 92.3992.641062.500.270.1693245
MC029 86.0373.33441.670.270.22150.3
MC899 104.79111.25902.250.250.1822820
MC698 107.90115.40653.710.230.15868
MC935 80.7176.28491.120.290.203459
MC696 54.7763.062266.000.340.1843213
MC800 50.4275.65511.000.270.20110.3
MC682 28.5355.83891.500.300.201958
MC778 54.5370.001009.880.300.2071973
MC807 57.3461.67392.710.300.284445427
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Hu, X.; Bhattacherjee, R.; Botchway, K.; Pashin, J.C.; Chakraborty, G.; Bikkina, P. CO2 Storage Site Analysis, Screening, and Resource Estimation for Cenozoic Offshore Reservoirs in the Central Gulf of Mexico. Energies 2024, 17, 1349. https://doi.org/10.3390/en17061349

AMA Style

Hu X, Bhattacherjee R, Botchway K, Pashin JC, Chakraborty G, Bikkina P. CO2 Storage Site Analysis, Screening, and Resource Estimation for Cenozoic Offshore Reservoirs in the Central Gulf of Mexico. Energies. 2024; 17(6):1349. https://doi.org/10.3390/en17061349

Chicago/Turabian Style

Hu, Xitong, Rupom Bhattacherjee, Kodjo Botchway, Jack C. Pashin, Goutam Chakraborty, and Prem Bikkina. 2024. "CO2 Storage Site Analysis, Screening, and Resource Estimation for Cenozoic Offshore Reservoirs in the Central Gulf of Mexico" Energies 17, no. 6: 1349. https://doi.org/10.3390/en17061349

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