1. Field of the Invention
The present invention relates to techniques for performing oilfield operations relating to subterranean formations having reservoirs therein.
More particularly, the invention relates to techniques for performing oilfield operations involving an analysis of reservoir, cap rock, overburden, and other geological structures in the subterranean formations, and their impact on such oilfield operations.
2. Background of the Related Art
Oilfield operations, such as surveying, drilling, wireline testing, completions, simulation, planning and oilfield analysis, are typically performed to locate and gather valuable downhole fluids. Various aspects of the oilfield and its related operations are shown in
As shown in
After the drilling operation is complete, the well may then be prepared for simulation. As shown in
During the oilfield operations, data is typically collected for analysis and/or monitoring of the oilfield operations. Such data may include, for example, subterranean formation, equipment, historical and/or other data. Data concerning the subterranean formation is collected using a variety of sources. Such formation data may be static or dynamic. Static data relates to, for example, formation structure and geological stratigraphy that define the geological structure of the subterranean formation. Dynamic data relates to, for example, fluids flowing through the geologic structures of the subterranean formation over time. Such static and/or dynamic data may be collected to learn more about the formations and the valuable assets contained therein.
Sources used to collect static data may be seismic tools, such as a seismic truck that sends compression waves into the earth as shown in
Such well logging may be performed using, for example, the drilling tool of
Sensors may be positioned about the oilfield to collect data relating to various oilfield operations. For example, sensors in the drilling equipment may monitor drilling conditions, sensors in the wellbore may monitor fluid composition, sensors located along the flow path may monitor flow rates, and sensors at the processing facility may monitor fluids collected. Other sensors may be provided to monitor downhole, surface, equipment or other conditions. The monitored data is often used to make decisions at various locations of the oilfield at various times. Data collected by these sensors may be further analyzed and processed. Data may be collected and used for current or future operations. When used for future operations at the same or other locations, such data may sometimes be referred to as historical data.
The processed data may be used to predict downhole conditions, and make decisions concerning oilfield operations. Such decisions may involve well planning, well targeting, well completions, operating levels, simulation rates and other operations and/or conditions. Often this information is used to determine when to drill new wells, re-complete existing wells, or alter wellbore simulation.
Data from one or more wellbores may be analyzed to plan or predict various outcomes at a given wellbore. In some cases, the data from neighboring wellbores or wellbores with similar conditions or equipment may be used to predict how a well will perform. There are usually a large number of variables and large quantities of data to consider in analyzing oilfield operations. It is, therefore, often useful to model the behavior of the oilfield operation to determine the desired course of action. During the ongoing operations, the operating conditions may need adjustment as conditions change and new information is received.
Techniques have been developed to model the behavior of various aspects of the oilfield operations, such as geological structures, downhole reservoirs, wellbores, surface facilities as well as other portions of the oilfield operation. Examples of these modeling techniques are shown in Patent/Publication/Application Nos. U.S. Pat. No. 5,992,519, WO2004/049216, WO1999/064896, WO2005/122001, U.S. Pat. No. 6,313,837, US2003/0216897, US2003/0132934, US2005/0149307, US2006/0197759, U.S. Pat. No. 6,980,940, US2004/0220846, and Ser. No. 10/586,283.
Techniques have also been developed for performing reservoir simulation operations. See, for example, Patent/Publication/Application Nos. U.S. Pat. No. 6,230,101, U.S. Pat. No. 6,018,497, U.S. Pat. No. 6,078,869, GB2336008, U.S. Pat. No. 6,106,561, US2006/0184329, U.S. Pat. No. 7,164,990. Some simulation techniques may involve an analysis of gas and its effects on the oilfield operation. See, for example U.S. Pat. No. 7,069,148. Some simulation techniques involve the use of coupled simulations as described, for example, in Publication No. US2006/0129366.
Despite the development and advancement of reservoir simulation techniques in oilfield operations, there remains a need to consider the effects of gas on oilfield operations. It would be desirable to provide techniques for selecting, planning and/or implementing gas operations based on static and dynamic aspects of the oilfield. It is further desirable that such techniques selectively consider desired parameters, such as chemistry, transport, mechanics and heat. Such desired techniques may be capable of one of more of the following, among others: providing modeling capability for a variety of subsurface formations (such as oil field, gas field, brine reservoir, aquifer, etc.), providing coupling capability of static model, dynamic model, etc. in the simulator, providing coupling capability among various physico-chemical mechanisms, providing feedback to permit adjustment of desired portions of the oilfield and/or gas operation, providing planning (i.e., development plan, operational plan, monitoring plan, etc.) based on simulation results.
In general, in one aspect, the invention relates to a method of performing a gas operation of an oilfield having a subterranean formation with at least one reservoir positioned therein. The method steps include modeling the gas operation of the oilfield using a multi-domain simulator by coupling a static model of the subterranean formation, a dynamic model of the subterranean formation, and a well model, wherein the multi-domain simulator comprises the static model, the dynamic model, and the well model, defining a development plan for the gas operation based on the modeling, and performing gas injection according to the development plan.
In general, in one aspect, the invention relates to a method of performing a gas operation of an oilfield having a subterranean formation with at least one reservoir positioned therein. The method steps include modeling the gas operation of the oilfield using a multi-domain simulator by coupling a static model of the subterranean formation, a dynamic model of the subterranean formation, and a well model, wherein the multi-domain simulator comprises the static model, the dynamic model, and the well model, acquiring at least one selected from a group consisting of survey data and monitoring data from the subterranean formation, providing a feedback based on comparing simulation data from the multi-domain simulator to the at least one selected from a group consisting of survey data and monitoring data, and performing the gas operation according to the feedback.
In general, in one aspect, the invention relates to a method of performing a gas operation of an oilfield having a subterranean formation with at least one reservoir positioned therein. The method steps include modeling the gas operation of the oilfield using a multi-domain simulator by coupling a static model of the subterranean formation, a dynamic model of the subterranean formation, and a well model, wherein the multi-domain simulator comprises the static model, the dynamic model, and the well model, performing an economic assessment based on the modeling, and performing the gas operation according to the economic assessment.
In general, in one aspect, the invention relates to a computer readable medium, embodying instructions executable by a computer to perform method steps for a gas operation of an oilfield having a subterranean formation with at least one reservoir positioned therein. The instructions include functionality to model the gas operation of the oilfield using a multi-domain simulator by coupling a static model of the subterranean formation, a dynamic model of the subterranean formation, and a well model, wherein the multi-domain simulator comprises the static model, the dynamic model, and the well model, to define a development plan for the gas operation based on the modeling, and to perform gas injection according to the development plan.
In general, in one aspect, the invention relates to a computer readable medium embodying instructions executable by a computer to perform method steps for computer readable medium, embodying instructions executable by a computer to perform method steps for a gas operation of an oilfield having a subterranean formation with at least one reservoir positioned therein. The instructions include functionality to model the gas operation of the oilfield using a multi-domain simulator by coupling a static model of the subterranean formation, a dynamic model of the subterranean formation, and a well model, wherein the multi-domain simulator comprises the static model, the dynamic model, and the well model, to acquire at least one selected from a group consisting of survey data and monitoring data from the subterranean formation, to provide a feedback based on comparing simulation data from the multi-domain simulator to the at least one selected from a group consisting of survey data and monitoring data, and to perform the gas operation according to the feedback.
Other aspects and advantages of the invention will be apparent from the following description and the appended claims.
So that the above recited features and advantages of the present invention can be understood in detail, a more particular description of the invention, briefly summarized above, may be had by reference to the embodiments thereof that are illustrated in the appended drawings. It is to be noted, however, that the appended drawings illustrate only typical embodiments of this invention and are therefore not to be considered limiting of its scope, for the invention may admit to other equally effective embodiments.
Presently preferred embodiments of the invention are shown in the above-identified figures and described in detail below. In describing the preferred embodiments, like or identical reference numerals are used to identify common or similar elements. The figures are not necessarily to scale and certain features and certain views of the figures may be shown exaggerated in scale or in schematic in the interest of clarity and conciseness.
In response to the received sound vibration(s) (112) representative of different parameters (such as amplitude and/or frequency) of the sound vibration(s) (112). The data received (120) is provided as input data to a computer (122a) of the seismic recording truck (106a), and responsive to the input data, the recording truck computer (122a) generates a seismic data output record (124). The seismic data may be further processed as desired, for example by data reduction.
A surface unit (134) is used to communicate with the drilling tool (106b) and offsite operations. The surface unit (134) is capable of communicating with the drilling tool (106b) to send commands to drive the drilling tool (106b), and to receive data therefrom. The surface unit (134) is preferably provided with computer facilities for receiving, storing, processing, and analyzing data from the oilfield (100). The surface unit (134) collects data output (135) generated during the drilling operation. Computer facilities, such as those of the surface unit (134), may be positioned at various locations about the oilfield (100) and/or at remote locations.
Sensors (S), such as gauges, may be positioned throughout the reservoir, rig, oilfield equipment (such as the downhole tool), or other portions of the oilfield for gathering information about various parameters, such as surface parameters, downhole parameters, and/or operating conditions. These sensors (S) preferably measure oilfield parameters, such as weight on bit, torque on bit, pressures, temperatures, flow rates, compositions and other parameters of the oilfield operation.
The information gathered by the sensors (S) may be collected by the surface unit (134) and/or other data collection sources for analysis or other processing. The data collected by the sensors (S) may be used alone or in combination with other data. The data may be collected in a database and all or select portions of the data may be selectively used for analyzing and/or predicting oilfield operations of the current and/or other wellbores.
Data outputs from the various sensors (S) positioned about the oilfield may be processed for use. The data may be historical data, real time data, or combinations thereof. The real time data may be used in real time, or stored for later use. The data may also be combined with historical data or other inputs for further analysis. The data may be housed in separate databases, or combined into a single database.
The collected data may be used to perform analysis, such as modeling operations. For example, the seismic data output may be used to perform geological, geophysical, reservoir engineering, and/or production simulations. The reservoir, wellbore, surface and/or process data may be used to perform reservoir, wellbore, or other production simulations. The data outputs from the oilfield operation may be generated directly from the sensors (S), or after some preprocessing or modeling. These data outputs may act as inputs for further analysis.
The data is collected and stored at the surface unit (134). One or more surface units (134) may be located at the oilfield (100), or linked remotely thereto. The surface unit (134) may be a single unit, or a complex network of units used to perform the necessary data management functions throughout the oilfield (100). The surface unit (134) may be a manual or automatic system. The surface unit (134) may be operated and/or adjusted by a user.
The surface unit (134) may be provided with a transceiver (137) to allow communications between the surface unit (134) and various portions of the oilfield (100) or other locations. The surface unit (134) may also be provided with or functionally linked to a controller for actuating mechanisms at the oilfield. The surface unit (134) may then send command signals to the oilfield (100) in response to data received. The surface unit (134) may receive commands via the transceiver or may itself execute commands to the controller. A processor may be provided to analyze the data (locally or remotely) and make the decisions to actuate the controller. In this manner, the oilfield (100) may be selectively adjusted based on the data collected to optimize fluid recovery rates, or to maximize the longevity of the reservoir and its ultimate production capacity. These adjustments may be made automatically based on computer protocol, or manually by an operator. In some cases, well plans may be adjusted to select optimum operating conditions, or to avoid problems.
The wireline tool (106c) may be operatively linked to, for example, the geophones (118) stored in the computer (122a) of the seismic recording truck (106a) of
Sensors (S), such as gauges, may be positioned about the oilfield to collect data relating to various oilfield operations as described previously. As shown, the sensor (S) may be positioned in the production tool (106d) or associated equipment, such as the Christmas tree, gathering network, surface facilities and/or the production facility, to measure fluid parameters, such as fluid composition, flow rates, pressures, temperatures, and/or other parameters of the production operation.
While only simplified wellsite configurations are shown, it will be appreciated that the oilfield may cover a portion of land, sea and/or water locations that hosts one or more wellsites. Production may also include injection wells (not shown) for added recovery. One or more gathering facilities may be operatively connected to one or more of the wellsites for selectively collecting downhole fluids from the wellsite(s).
While
The oilfield configuration in
The respective graphs of
Data plots (308a-308c) are examples of static data plots that may be generated by the data acquisition tools (302a-302d), respectively. Static data plot (308a) is a seismic two-way response time and may be the same as the seismic trace (202) of
The subterranean formation (304) has a plurality of geological structures (306a-306d). As shown, the formation has a sandstone layer (306a), a limestone layer (306b), a shale layer (306c), and a sand layer (306d). A fault line (307) extends through the formation. The static data acquisition tools are preferably adapted to measure the formation and detect the characteristics of the geological structures of the formation.
While a specific subterranean formation (304) with specific geological structures are depicted, it will be appreciated that the formation may contain a variety of geological structures. Fluid may also be present in various portions of the formation. Each of the measurement devices may be used to measure properties of the formation and/or its underlying structures. While each acquisition tool is shown as being in specific locations along the formation, it will be appreciated that one or more types of measurement may be taken at one or more location across one or more oilfields or other locations for comparison and/or analysis. Further, these measurements do not only elucidate the state of rock and fluids once in time, but also detect and quantify changes in rock and fluids properties with time through carefully designed periodic measurements and surveys.
The data collected from various sources, such as the data acquisition tools of
Each wellsite (402) has equipment that forms a wellbore (436) into the earth. The wellbores extend through subterranean formations (406) including reservoirs (404). These reservoirs (404) contain fluids, such as hydrocarbons. The wellsites draw fluid from the reservoirs and pass them to the processing facilities via gathering networks (444). The gathering networks (444) have tubing and control mechanisms for controlling the flow of fluids from the wellsite to the processing facility (454).
Wellbore simulation equipment (564) extends from a wellhead (566) of wellsite (402) and to the reservoir (404) to draw fluid to the surface. The wellsite (402) is operatively connected to the gathering network (444) via a transport line (561). Fluid flows from the reservoir (404), through the wellbore (436), and onto the gathering network (444). The fluid then flows from the gathering network (444) to the process facilities (454).
As further shown in
As shown in
The analyzed data may then be used to make decisions. A transceiver (not shown) may be provided to allow communications between the surface unit (534) and the oilfield (400). The controller (522) may be used to actuate mechanisms at the oilfield (400) via the transceiver and based on these decisions. In this manner, the oilfield (400) may be selectively adjusted based on the data collected. These adjustments may be made automatically based on computer protocol and/or manually by an operator. In some cases, well plans are adjusted to select optimum operating conditions or to avoid problems.
A display unit (526) may be provided at the wellsite (402) and/or remote locations for viewing oilfield data (not shown). The oilfield data represented by a display unit (526) may be raw data, processed data and/or data outputs generated from various data. The display unit (526) is preferably adapted to provide flexible views of the data, so that the screens depicted may be customized as desired. A user may determine the desired course of action during simulation based on reviewing the displayed oilfield data. The simulation operation may be selectively adjusted in response to the display unit (526). The display unit (526) may include a two dimensional display for viewing oilfield data or defining oilfield events. For example, the two dimensional display may correspond to an output from a printer, plot, a monitor, or another device configured to render two dimensional output. The display unit (526) may also include a three-dimensional display for viewing various aspects of the simulation operation. At least some aspect of the simulation operation is preferably viewed in real time in the three-dimensional display. For example, the three dimensional display may correspond to an output from a printer, plot, a monitor, or another device configured to render three dimensional output.
To facilitate the processing and analysis of data, simulators may be used to process the data. Specific simulators are often used in connection with specific oilfield operations, such as reservoir or wellbore simulation. Data fed into the simulator(s) may be historical data, real time data or combinations thereof. Simulation through one or more of the simulators may be repeated or adjusted based on the data received.
As shown, the oilfield operation is provided with wellsite and non-wellsite simulators. The wellsite simulators may include a reservoir simulator (549), a wellbore simulator (592), and a surface network simulator (594). The reservoir simulator (549) solves for hydrocarbon flow through the reservoir rock and into the wellbores. The wellbore simulator (592) and surface network simulator (594) solves for hydrocarbon flow through the wellbore and the surface gathering network (444) of pipelines. As shown, some of the simulators may be separate or combined, depending on the available systems.
The non-wellsite simulators may include process and economics simulators. The processing unit has a process simulator (548). The process simulator (548) models the processing plant (e.g., the process facility (454)) where the hydrocarbon is separated into its constituent components (e.g., methane, ethane, propane, etc.) and prepared for sales. The oilfield (400) is provided with an economics simulator (547). The economics simulator (547) models the costs of part or all of the oilfield throughout a portion or the entire duration of the gas operation. Various combinations of these and other oilfield simulators may be provided.
The site selection stage (601) involves a review of potential sites A, B, and C of an oilfield that may be used for disposal of gas. In one or more embodiments of the invention, the oilfield may be any geographical region having geological structures (e.g., saline aquifers, brine reservoirs, hydrocarbon reservoirs, other fluid bodies or cavities, etc.) capable of receiving and storing the gas. During site selection, data is collected and processed for each of the sites, an initial risk identification, and assessment survey is made. Then, each site is modeled to determine its viability as a disposal site. A multi-domain simulator (620) is used to model site A, site B, and site C for ranking and selective targeting gas disposal site, e.g., site A.
Once the site is selected, the planning stage is performed (602). During the planning stage, a survey plan (610) is developed to acquire survey data (611) for updating the modeling and defining the development plan (613) to generate the well configuration (614) and the surface facility design (616).
Once the site is planned, the implementation stage is performed (603). During the implementation stage, the drilling operation and/or injection operation (615) are performed based on the well configuration (614). Surface facilities are designed and built. The gas produced from the gas source (617) is disposed on the surface facilities (616).
As shown in
In the example depicted, three sites (i.e., site A, site B, and site C) are considered for disposing the carbon dioxide produced from the gas source (617). The sites are evaluated to determine their ability to store the CO2. Various considerations, such as the static, dynamic, and wellbore characteristics as well as likelihood of associated identified risks may be considered in site selection.
The multi-domain simulator (620) is used to evaluate the static, dynamic, and wellbore characteristics. As shown, a static model (604) is used to evaluate the static or geological characteristics of each of the sites. The geological structure of a given site may include the various underground formations, such as rock layers, faults, coal beds, associated cap rock formations and other structures, contained in the site. In many cases, the formation may include mostly sedimentary deposits having porosity suitable for gas storage.
A well model (630) is also used to evaluate the wellbore characteristics of the sites. The wellbore characteristics relate to the shape, direction and other features (e.g. completion) of the wellbore that may affect the flow of fluid therethrough. Such features may affect, for example, the ability to transport gas to a particular location.
A dynamic model (608) is also used to evaluate the reservoir or dynamic characteristics of reservoirs within the various sites including geological formations overlaying the reservoir (e.g., cap rock or overburden). The sites have saline aquifers, brine reservoirs, hydrocarbon reservoirs, and other fluid bodies or cavities capable of receiving and storing the gas. Such features, such as capacity, may affect the ability of a reservoir to store the gas.
Preferably, the models used to perform the site selection are coupled to provide the overall best solution based on all the models. The operation of the various model and the coupling of these models are described in further detail with respect to
In the example shown in
Analysis based on the performance categories overlays the entire gas operation and may be performed at any point in the operation or for the entire operation.
Once the site selection stage is complete, the planning stage (602) may begin. With the target disposal site selected, survey data (611) is acquired from the selected site to update one or more of the models (612). A development plan (613) is then defined based on modeling the gas operation using the multi-domain simulator (620) with the updated model(s), such as the static model (612), well model (630) and/or dynamic model (608). The development plan (613) may provide well location, well design, drilling plan, gas injection plan, monitoring plan, etc. The planning stage is described in greater detail below with respect to
Once the planning stage is complete and a plan is defined, the implementation stage (603) may begin. The implementation stage (603) takes action based on the development plan (613) provided. The development plan (613) defines the operating parameters (614), such as well location and well design. The development plan also defines the drilling and/or injection operation (615), such as the equipment and drilling parameters for drilling the well to the desired site. The implementation stage (603) is described in greater detail with respect to
As an example, site A, as shown in
The multi-domain simulator (620) includes the static model (604) and the dynamic model (608). The monitoring data (711) (e.g., well logs, well testing, etc.) is provided to update the static model (604) and the dynamic model (608), which is based on the previous knowledge and survey data of subsurface geological make up in modeling the site selection stage and pre-drilling stage as illustrated in
Key parameters (713) of the injection operation (e.g., the injection interval, injection cycle, injection rate, etc.) are simulated to evaluate the response (714) before the injection plan (716) is finalized. Monitoring plan (715) is devised for acquiring monitoring data (711) from the monitoring instrument (704) and monitoring instrument (710).
Regarding the injection plan (716), injection scenarios can be simulated in selected sections (e.g., I1 (717), I2 (718), etc.) to select the best injection interval and injection strategy (e.g., continuous injection, interval injection, water-alternating (WAG) injection, etc.). The result supports operational decisions such as using a single well for injection or setting up a multi-well operation (e.g. including injection well W1 (701) and injection well W3 (705), but excluding injection well W2 (703)). Also, at the pre-injection stage, with the properties of the subsurface fluids (e.g., brine) known, eventual problems or benefits (e.g., caused by dry-out, salting out, induced chemical reactions, etc.) can be evaluated and mitigation strategies tested. Similar simulations can also aid the design and placement of monitoring equipment in the monitoring well (702).
Regarding the monitoring plan (715), the prediction of the behavior of the CO2 (e.g., displacement of the plume, trapping mechanisms, etc.) allows an optimum monitoring strategy to be defined for controlling the performance of the gas disposal site with respect to the storage objective. For example, measurement techniques and appropriate sensors may be selected for being sensitive to a certain gas presence or changes in reservoir properties (e.g., pressure) due to gas injection. This selection is performed using tool response models (not shown) representing the instruments and sensors (e.g., monitoring instrument (704) and/or monitoring instrument 710) coupled with the simulators (e.g., static model (604) and the dynamic model (608)) in the multi-domain simulator (620). Further, the monitoring plan (715) also includes planning monitoring wells (e.g., monitoring well (702)), such as designing surface survey, surface-to-borehole survey, or borehole measurement surveys. These surveys can be included in the multi-domain simulator (620) to evaluate the efficacy to finalize the monitoring plan (715).
The gas disposal site (720) includes the aquifer (709) located about the subterranean formation (706) and monitoring instruments (704) shown in
For example, outputs from the dynamic model (608), such as pressure and saturation distributions, are inputs for tool response modeling (i.e., resistivity, seismic, gravity survey, etc.). Noticeable discrepancies between predicted and actual tool measurements allow updating model parameters, such as properties or geometry.
The mismatch between observation data and predictions is generally due to an oversimplified reservoir model. In that case, the model is refined and parameters are added until predictions agree with observations. Repeated history matching exercises allow models to be updated and further refined. This workflow loop can be repeated during the whole injection operation lifetime. Recorded changes in behavior can be simulated to better understand the parameters responsible for deviations and the consequences of adjustments of operation parameters, such as well shut-in, changes in injection rates, work-overs, etc.
Further as shown in
As knowledge in the reservoir is increased (e.g., based on the repeated history matching exercises described above), additional risk assessment scenarios (903) (e.g., gas escape and leakage scenario, etc.) may be modeled for the purpose of understanding and assessing risk of the gas injection operation. This also supports devising remediation strategies (904) (e.g., mitigation) and testing its potential effectiveness in models before implementation.
During the operation (cessation of injection, also referred to in
Even after abandonment, longer term monitoring continues and the data is incorporated into models that can be updated should changes in the subsurface conditions be detected. Also in case of larger deviations caused by unexpected and unplanned events (e.g., leakage, early attainment of max pressure, etc.), models can be used to plan and assess mitigation actions.
In addition to the site selection, characterization, planning, implementation, and risk assessment stages of the gas operation (600), shut down/retirement stage involves shutting down operations, for example, for preparing the field for retirement or extracting the gas at a later time for use elsewhere. Retirement strategy and abandonment plan/actions on facilities are designed using modeling techniques described above. For instance, if after several years of shut-in phase (injection stop), the monitoring system still records significant changes in reservoir parameters, these data may be used to decide on an extension of the shut-in phase. The retirement strategy may include treating the reservoir chemically by injecting specific engineered fluids to isolate the near wellbore area over the very long term. Simulations will indicate how to best perform these operations for obtaining the desired result.
Multiple disciplines, or aspects, are addressed in modeling the gas operation within the multi-domain simulator (620). These disciplines include TRANSPORT (e.g., of fluids, chemicals, heat, etc.), HEAT (e.g., temperature changes, energy sources and sinks, etc.), MECHANICS (e.g., pressure impact, fracturing, etc.), CHEMISTRY (e.g., thermodynamics, chemical reactions affecting material properties, etc.), etc. Key parameters and dependencies in these disciplines are coupled in complex ways, e.g., the density of materials (such as rocks, fluids, well completion materials, etc.) changes with variations of temperature (HEAT), pressure (MECHANICS), chemical reactions (CHEMISTRY), transport and mixing with other materials (TRANSPORT). Performance of the gas operation in capacity, injectivity, containment, economics, or other categories are modeled by coupling mathematical equations representing each discipline in an integrated system. Subsystems (i.e., portions or limited aspects of the gas operation) are modeled by portions of these mathematical equations. These mathematical equations represent coupled processes in these disciplines that are simulated accurately for selected subsystems and integrated for full system analysis. For example, the relevant processes modeled in these categories are described in the following paragraphs.
Storage capacity and trapping mechanisms are modeled in the capacity category. For example, trapping mechanism kinetics, such as structural/hydrodynamics, solubility, residual phase, mineralization/absorption, etc., are modeled. Further, storage properties evolution, such as CO2 saturation, dissolved CO2, pressure, pH, etc., are modeled for model parameter calibration using monitoring measurements.
Injectivity relates to injection optimization near a wellbore in the gas disposal site. Injection-induced temperature variations, pressure increase, and chemical reactions (e.g., salt precipitation, CaCO3 dissolution/precipitation) and their effects on porosity, permeability, and mechanical properties (e.g., stresses to control subsidence in case of carbonate dissolution and to control completion integrity) are modeled in this category. Near wellbore properties (e.g., temperature profile, pressure, CO2 saturation, pH and other properties) are modeled for comparison with monitoring measurements and further calibration of the simulator parameters. Injection cycles are modeled in injecting CO2 alternated with another substance to maintain well injectivity. Further, the network of injection wells (e.g., number, trajectory, etc.) is modeled and optimized to ensure long-term stability of injection capabilities at the lowest cost and to minimize the risks of leakage. Effect of impurities in the gas stream may also be modeled. For all the above aspects of the injectivity modeling, the local grid may be refined manually or automatically for detailed analysis of near wellbore conditions.
In the containment category, the effects of pressure increase on storage seal integrity (e.g., caused by fault-reactivation, cap rock fracturing, and/or over pressuring the reservoir) are modeled. Reactive transport in cap rock formation and in fault gouge/cement materials (primary seal) is also modeled. CO2 seepage in the overburden (including vadose zone) and trapping mechanisms along these leakage routes is modeled to assess impact and to devise mitigation for shallow fresh water resources. Modeling in the containment category is coupled to responses of environmental surface monitoring.
Using simplified geological models based on previous knowledge of subsurface geological make up (e.g., of site A, site B, and site C) simulation of CO2 injection provides pre-selection capacity estimation, which is one of the ranking criteria for site selection. Further, a development plan for the gas operation is modeled. As described above, the development plan includes well location, well design, drilling plan, gas injection plan, monitoring plan, etc. The modeled injection strategy (e.g., number of wells, type of wells, injection rates, etc.) and surface considerations (e.g., distance from CO2 source, transport mode, accessibility to facilities and storage site) allow first order assessment of economics.
In modeling the chemistry aspect (1001) in
The various stages of the gas operation described in
Turning to
The multi-domain coupling module (1006) simplifies the interacting mechanisms between the transport aspect (1002) and the mechanics aspect (1003) to address stress, rock strength, pressure, porosity, permeability, etc.
The multi-domain coupling module (1007) simplifies the interacting mechanisms between the transport aspect (1002) and the heat aspect (1004) to address advective or convective heat transport, pressure, porosity, permeability, density, viscosity, etc.
The multi-domain coupling module (1008) simplifies the interacting mechanisms between the mechanics aspect (1003) and the heat aspect (1004) to address frictional heating, thermal expansion, stress, rock strength, pressure, porosity, permeability, etc.
The multi-domain coupling module (1009) simplifies the interacting mechanisms between the chemistry aspect (1001) and the heat aspect (1004) to address temperature change, endothermic/exothermic reactions, reaction rates, phase changes, Joule-Thompson thermal effect, etc.
The multi-domain coupling module (1010) simplifies the interacting mechanisms between the mechanics aspect (1003) and the chemistry aspect (1001) to address frictional heat induced chemical reaction, structural impact from chemical reaction, pressure, porosity, permeability, density, viscosity, etc.
Now turning to
Each multi-domain coupling module is customized for a specific problem to achieve computational efficiency. Specific problems may include certain physical and chemical processes in the subsurface induced by the presence of CO2 (and associated gases) either through deliberate injection for sequestration and/or enhanced oil recovery (EOR) or due to natural occurrence. Examples include thermodynamic equilibration of the various phases, model for capillary pressure and relative permeability hysteresis, models for the dissolution and precipitation of salts and minerals, chemical reactions of these components and adsorption/desorption mechanisms for gases (e.g. CH4/CO2) as well as shrinkage/swelling of coals, mechanical compression of rock matrix, etc.
As an example, the multi-domain coupling module (1005) and (1054) is customized for the specific problem relating to CO2 injection into a brine reservoir described below. During dry CO2 injection in saline aquifers, the near wellbore environment is driven to residual water saturation. Over a period of time, governed by the mass transfer of water into the CO2 rich phase, the formation water is evaporated causing dissolved salt to precipitate in the pore spaces. This reduces the porosity and decreases the permeability of the formation to CO2. This coupling between chemistry aspect (1001) (i.e., mutual solubility between water and CO2) and transport aspect (1002) (i.e., the decrease in the permeability of the formation to CO2) is modeled by the multi-domain coupling module (1005) in the following manner. The near wellbore environment is modeled as a multi-phase system of CO2 and H2O partitioned in a CO2-rich and H2O-rich phase, including, for example, the four components:
CO2—liquid/vapour component
H2O—liquid/vapour component
NaCl—liquid/solid component
CaCl2—liquid/solid component
The salt concentrations are assumed to vary slowly so the partial derivatives of the phase splitting with respect to the salt concentrations are set to zero in the Jacobian used for iterative updating. This reduces the computational overhead.
An exemplary algorithm for phase compositional computations is described below. Given the molar density mi of each component, the pressure P, and the temperature T, the compositions are calculated in the following steps.
Do until change in S, L, V, xi, yi and si<Tolerance (a predetermined number)
Set XH2O=1.0−XCO2−xsalt
K
CO2
=Y
CO2
/X
CO2
K
H2O
=Y
H2O
/X
H2O
K
NaCl=1E−12 (small number)
K
CACL2=1E−12
Set vapour-liquid feed zVLi=(zi−S*si)/(1−S)
The solid saturation can be transformed into volume of salt precipitated indicating the associated reduction in porosity. The impact of the porosity change on permeability (and flow) is described with a mobility impact factor that may be calibrated on laboratory data by the user.
When CO2 is injected, the salt concentration in water increases because water is evaporated from the brine into the CO2 phase. Another case is when pressure and temperature change cause a modification of the solubility of various salts resulting in existing salts being dissolved or precipitated. This can ultimately lead to precipitation of salt when the concentration of NaCl exceeds a salination limit, i.e., the maximum NaCl solubility. This limit depends on the presence of other salts, e.g., CaCl2. Thermodynamic calculations within a compositional simulator are carried out for each grid block. These calculations are computational resource intensive and may multiply the computational time by a large factor. In an example, the multi-domain coupling module (1001) is customized to use explicit expressions to circumvent the large scale iterative calculation. These explicit expressions are customized for modeling the NaCl precipitation. Different salts (other than NaCl) or different equilibria (other than precipitation) require different explicit expressions. The maximum NaCl solubility in water is pre-calculated separately using a chemical speciation software. The results are fit to a curve fitting function (e.g., Pade approximation) that takes both temperature and CaCl2 into account. An explicit relationship for NaCl precipitation in the formation as a function of mole fraction of CaCl2 and temperature is obtained.
The thermodynamic calculations are simplified.
The conservation of total NaCl in a grid cell i is then given by the equation
where VP is the pore volume, Fi->j denotes the flow of water NaCl in/out from cell i to cell j and Qw is a source sink term representing wells.
Additional to the precipitation problem in the near wellbore environment, modeled using the customized multi-domain coupling module (1005) described above, the impact of dissolution and precipitation in the rock may change the pore space geometry in the rock and can change fundamentally the space available for fluids to move and impact pressures in the reservoir and the wells. The mapping of porosity changes into permeability changes is another example of a specific problem to be modeled by customizing the multi-domain coupling module (1001). The results can lead to the necessity of adjustments of the surface facilities to ensure continuation of the gas operation.
Furthermore, time dependent processes and transient processes exhibited in the CO2 injection into a brine reservoir are modeled by customizing the multi-domain coupling module (1054) in a similar fashion based on the above description.
As another example, the multi-domain coupling module (1005) for modeling CO2 injection (or gas mixtures) into a coal bed is customized for the specific problem described below. One of the geological storage options is to inject CO2 into coal beds containing methane. Methane is preferentially released and CO2 adsorbed. The multi-domain coupling module (1005) is customized for modeling coal shrinkage/swelling effects when injecting CO2 into coal seams.
A rock compaction model based on the Palmer and Mansoori model has the weakness of predicting volumetric strain due to swelling/shrinkage even if no coal gas is adsorbing or desorbing. The multi-domain coupling module (1005) for modeling CO2 injection into a coal bed may be customized to use the fracture pressure and composition together with an extended Langmuir curve parameter model. Pore volume multiplier is constructed from a combination of a compression term and a swelling/shrinkage term, such as
V
m=1+C0(P−P0)+Ce(ε−ε0)
This approach, due to the computations of ε0 as described below, does not predict shrinkage/swelling when the gas adsorbed is not changing.
The component strain is then calculated by an extended Langmuir
formula:
where ε∞,k and bk are input Langmuir curve parameters for component k, ak represent the adsorbed mole fraction and Psorb is the sorption pressure. The sorption pressure is defined as the fracture pressure if there is a free gas-phase; if not a free gas-phase, the sorption pressure is the pressure when the gas phase begins to desorb. The sorption pressure and corresponding equilibrium mole fractions can be calculated and the total strain is calculated by:
In addition, geomechanical processes fundamental to understand and operate CO2 injection into coal bed with or without enhanced methane production can be expanded and added into the customized multi-domain coupling module (1005).
Furthermore, threshold events relating to rock compaction or fracturing associated with CO2 injection into a coal bed during the injection stage, risk assessment, or abandonment strategy are addressed by the multi-domain coupling module (1054) for modeling the interaction between the dynamic model (608) and the static model (604).
A plurality of estimated characteristics of the disposal site is determined based on the modeling, where the variety of estimated characteristics include at least one selected from a group including capacity, injectivity, containment, and economics (Step 1103). The disposal site for gas disposal is selectively targeted based on comparing the plurality of estimated characteristics to a pre-determined criteria (Step 1104). This pre-determined criteria may be any appropriate threshold value for one or more of the plurality of estimated characteristics.
Survey data from the subterranean formation may be acquired at the disposal site (Step 1105). The survey data may be acquired in any appropriate manner described above, including both static and real-time acquisition techniques. Next, the static model and the dynamic model of the subterranean formation may be updated (as needed) based on the survey data (Step 1106).
A development plan is defined for the gas disposal according to the model updating, where the development plan includes at least one selected from a group including a well location, a well design, a drilling plan, a gas injection plan, and a monitoring plan (Step 1107).
Optionally, monitoring data may be acquired by executing the development plan (Step 1108). Acquisition of the monitoring data may be performed in a similar manner as described above in relation to
The gas disposal may be modeled (using the essentially similar techniques as described above) while executing the gas injection plan based on simulation using the static model and the dynamic model of the subterranean formation, and the well model (Step 1110). Feedback may be provided based on comparing simulation data to monitoring data (Step 1111).
The feedback may take any useful tangible form, including storage to a computer readable medium and/or display via a monitor, a printer, or any other display device.
Turning to
Next, a development plan for the gas operation is defined based on the modeling (Step 1204). At this point, gas injection may be performed according to the development plan (Step 1206).
Further, survey and/or monitoring data is acquired from the subterranean formation (Step 1208) and feedback is provided based on comparing simulation data from the multi-domain simulator to the survey and/or monitoring data (Step 1210). Finally, gas injection is performed according to the feedback (Step 1212). This survey and/or monitoring data may be acquired while executing the development plan mentioned in Step 1206 or at any time in the gas operation. Although not shown, economic and/or risk assessment may also be determined during the gas operation.
It will be understood from the foregoing description that various modifications and changes may be made in the preferred and alternative embodiments of the present invention without departing from its true spirit. For example, the modeling modules included herein may be manually and/or automatically activated to perform the desired function. The activation may be performed as desired and/or based on data generated, conditions detected and/or analysis of results from gas injection operations. The processes in the multiple aspects may be of various spatial scales (microscopic or macroscopic) and temporal scales (seconds to minutes or decades).
This description is intended for purposes of illustration only and should not be construed in a limiting sense. The scope of this invention should be determined only by the language of the claims that follow. The term “comprising” within the claims is intended to mean “including at least” such that the recited listing of elements in a claim are an open group. “A,” “an” and other singular terms are intended to include the plural forms thereof unless specifically excluded.
This application claims priority under 35 U.S.C. §119(e) from Provisional Patent Application No. 60/936,461 filed Jun. 19, 2007.
Number | Date | Country | |
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60936461 | Jun 2007 | US |