CA2960997A1 - Coal bed methane extraction and carbon capture - Google Patents
Coal bed methane extraction and carbon capture Download PDFInfo
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- CA2960997A1 CA2960997A1 CA2960997A CA2960997A CA2960997A1 CA 2960997 A1 CA2960997 A1 CA 2960997A1 CA 2960997 A CA2960997 A CA 2960997A CA 2960997 A CA2960997 A CA 2960997A CA 2960997 A1 CA2960997 A1 CA 2960997A1
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- carbon dioxide
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 148
- 239000003245 coal Substances 0.000 title claims abstract description 112
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims description 20
- 229910052799 carbon Inorganic materials 0.000 title claims description 20
- 238000000605 extraction Methods 0.000 title description 11
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 186
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 93
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 93
- 238000000034 method Methods 0.000 claims abstract description 48
- 238000009826 distribution Methods 0.000 claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 238000003860 storage Methods 0.000 claims description 10
- 238000003795 desorption Methods 0.000 claims description 8
- 230000032258 transport Effects 0.000 claims description 7
- 239000000284 extract Substances 0.000 claims description 6
- 230000001143 conditioned effect Effects 0.000 claims description 4
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 230000003750 conditioning effect Effects 0.000 claims 1
- 238000002336 sorption--desorption measurement Methods 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 18
- 229930195733 hydrocarbon Natural products 0.000 description 13
- 150000002430 hydrocarbons Chemical class 0.000 description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 239000005431 greenhouse gas Substances 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000005755 formation reaction Methods 0.000 description 5
- 239000003345 natural gas Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 3
- 230000005611 electricity Effects 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000003129 oil well Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000010795 Steam Flooding Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 230000009919 sequestration Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/295—Gasification of minerals, e.g. for producing mixtures of combustible gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G5/00—Storing fluids in natural or artificial cavities or chambers in the earth
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B41/00—Equipment or details not covered by groups E21B15/00 - E21B40/00
- E21B41/005—Waste disposal systems
- E21B41/0057—Disposal of a fluid by injection into a subterranean formation
- E21B41/0064—Carbon dioxide sequestration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/70—Combining sequestration of CO2 and exploitation of hydrocarbons by injecting CO2 or carbonated water in oil wells
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Environmental & Geological Engineering (AREA)
- Mining & Mineral Resources (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
A method to establish an adsorption/desorption process by injecting carbon dioxide into a coal bed involves injecting a carbon dioxide stream in a coal bed such that it is adsorbed by the coal bed and such that methane stored in the coal bed is desorbed and displaced. The displaced methane is extracted and processed for distribution.
Description
COAL BED METHANE EXTRACTION AND CARBON CAPTURE
FIELD
[0001] This relates to a process that displaces and extracts methane from a coal bed by storing carbon dioxide delivered by compression such as from a pipeline such as the Alberta Carbon Trunk Line. The pipeline delivered carbon dioxide stream is injected into coal beds for sequestration and storage BACKGROUND
FIELD
[0001] This relates to a process that displaces and extracts methane from a coal bed by storing carbon dioxide delivered by compression such as from a pipeline such as the Alberta Carbon Trunk Line. The pipeline delivered carbon dioxide stream is injected into coal beds for sequestration and storage BACKGROUND
[0002] The generation of electricity in North America and in most parts of the world is primarily provided by the combustion of coal, a cheap and abundant fossil fuel. Coal is typically mined and transported to a power plant where it is processed before combustion. The coal is combusted in a furnace to generate heat for the production of high pressure dry steam. The produced dry and superheated steam drives a steam turbine generator to produce electricity.
Coal is a high carbon content fuel, therefore a large emitter of carbon dioxide as well as NOx and S0x, greenhouse gases (GHG). Rapidly increasing concentrations of GHG's in the atmosphere and emerging evidence of global warming is now triggering international action to reduce GHG's emissions into the atmosphere. The combustion of coal to generate electricity is identified as a main contributor of GHG emissions, resulting in industry action being taken to reduce GHG emissions from the use of coal combustion. Recently, the government of Alberta has mandated that coal usage for power generation be terminated by the year 2030.
Coal is a high carbon content fuel, therefore a large emitter of carbon dioxide as well as NOx and S0x, greenhouse gases (GHG). Rapidly increasing concentrations of GHG's in the atmosphere and emerging evidence of global warming is now triggering international action to reduce GHG's emissions into the atmosphere. The combustion of coal to generate electricity is identified as a main contributor of GHG emissions, resulting in industry action being taken to reduce GHG emissions from the use of coal combustion. Recently, the government of Alberta has mandated that coal usage for power generation be terminated by the year 2030.
[0003] Coal bed methane extraction provides an alternative method to recover energy from coal in a safe, efficient and environmentally acceptable manner. Coal bed methane extraction is typically employed in un-mineable coal beds. Conventional coal bed methane recovery methods are based on reservoir pressure reduction, where methane is desorbed from the coal surface by reducing the reservoir pressure.
[0004] In the current standard mode of coal bed methane extraction, wells are drilled into a coal bed. The methane is extracted by desorption from coal surfaces where the reservoir pressure is first decreased by dewatering. The decrease in pressure allows the methane to desorb from the coal and flow as a gas to the well. The gas is processed at surface and compressed in a natural gas pipeline network for delivery to markets. More recently, to enhance coal bed methane extraction new methods have been developed. As described by U.S.
patent no.
patent no.
5,085,274 (Puri et al.) entitled "Recovery of methane from solid carbonaceous subterranean of formations", U.S. patent no. 5,332,036 (Shirley et al.) entitled "Method of recovery of natural gases from underground coal formations" and U.S. patent no. 5,014,785 (Puri et al.) entitled "Methane production from carbonaceous subterranean formations", the use of carbon dioxide diluted with inert gases enhances coal bed methane recoveries by reducing the partial pressure of methane and injecting other gases such as nitrogen, resulted in a substantial increment in production.
SUMMARY
[0005]
There is provided a method and system for safely storing carbon dioxide, and for extracting stored methane and other volatile hydrocarbons in a coal bed. The method injects carbon dioxide into a coal bed in a condition to be sequestered and stored, and to extract stored methane in the coal bed. The conditions under which the carbon dioxide is injected will depend on one or more of: coal bed depth relative to pressure and methane extraction relative to temperature. The extracted methane and other volatile hydrocarbons may then be recovered, processed and routed to natural gas pipeline distribution systems.
SUMMARY
[0005]
There is provided a method and system for safely storing carbon dioxide, and for extracting stored methane and other volatile hydrocarbons in a coal bed. The method injects carbon dioxide into a coal bed in a condition to be sequestered and stored, and to extract stored methane in the coal bed. The conditions under which the carbon dioxide is injected will depend on one or more of: coal bed depth relative to pressure and methane extraction relative to temperature. The extracted methane and other volatile hydrocarbons may then be recovered, processed and routed to natural gas pipeline distribution systems.
[0006] As coal has a stronger affinity for carbon dioxide, it establishes an adsorption/desorption process where carbon dioxide displaces and frees the methane from the coal bed to be recovered, processed and distributed to natural gas pipeline distribution systems.
The objective of the method and system is to permit carbon dioxide to be sequestered and stored.
In one example, the proposed Alberta Carbon Trunk Pipeline may be used to transport carbon dioxide recovered due to local carbon-generating activities. The carbon dioxide may then be injected into coal beds to establish an adsorption/desorption process where carbon dioxide is stored in the coal bed by displacing methane and other volatile hydrocarbons, which may then be recovered and processed, such as for pipeline transport and distribution.
The objective of the method and system is to permit carbon dioxide to be sequestered and stored.
In one example, the proposed Alberta Carbon Trunk Pipeline may be used to transport carbon dioxide recovered due to local carbon-generating activities. The carbon dioxide may then be injected into coal beds to establish an adsorption/desorption process where carbon dioxide is stored in the coal bed by displacing methane and other volatile hydrocarbons, which may then be recovered and processed, such as for pipeline transport and distribution.
[0007] In one example, carbon dioxide recovered and delivered by pipeline is injected at desired pressure and temperature conditions into a coal bed for carbon dioxide adsorption and methane desorption, such that carbon dioxide is stored, and methane is extracted from the coal bed.
[0008] In one aspect, the process comprises the following steps:
(a) injecting carbon dioxide at optimum pressure and temperature for adsorption into a coal bed;
(b) displacing and producing methane by desorption of stored methane and other volatile hydrocarbons at optimum pressure and temperature in the coal bed; and (c) processing the coal bed extracted hydrocarbon gas.
(a) injecting carbon dioxide at optimum pressure and temperature for adsorption into a coal bed;
(b) displacing and producing methane by desorption of stored methane and other volatile hydrocarbons at optimum pressure and temperature in the coal bed; and (c) processing the coal bed extracted hydrocarbon gas.
[0009] The above described process may be used to store carbon dioxide and extract stored methane in a coal bed. The extracted methane is processed and distributed as a fossil fuel derived from coal. The process stores carbon dioxide and extracts stored methane in coal beds, thus contributing to the production of clean abundant energy from a very concentrated carbon fuel. The process is considered to be clean since coal can store two or more moles of carbon dioxide for every mole of methane displaced. Coal can store up to 10 moles of carbon dioxide per mole of methane stored in coal, thus making it a carbon negative process.
[0010] As will hereinafter be further described, carbon dioxide is first delivered by a pipeline, such as the Alberta Carbon Trunk Line, and injected for adsorption into a coal bed for storage and desorption of stored methane from the coal bed. The desorbed and extracted coal bed methane may then be processed for distribution. The process may be used to safely store carbon dioxide in a coal bed by adsorption and also, by desorption, extract and process the coal bed hydrocarbons for distribution as a result of the carbon dioxide being injected.
BRIEF DESCRIPTION OF THE DRAWING
BRIEF DESCRIPTION OF THE DRAWING
[0011] These and other features will become more apparent from the following description in which reference is made to the appended drawing, the drawing is for the purpose of illustration only and is not intended to in any way limit the scope of the invention to the particular embodiment or embodiments shown, wherein:
FIG. 1 is a schematic diagram of a pipeline delivered carbon dioxide stream injected into a coal bed for storage by adsorption and methane extraction by desorption. It includes a gas processing unit to treat the extracted coal bed hydrocarbons for distribution.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
FIG. 1 is a schematic diagram of a pipeline delivered carbon dioxide stream injected into a coal bed for storage by adsorption and methane extraction by desorption. It includes a gas processing unit to treat the extracted coal bed hydrocarbons for distribution.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0012] The method described may be used to safely store carbon dioxide that is produced, recovered and transported by pipeline in such as may occur in a carbon capture process by adsorbing carbon dioxide into a coal bed. It will be understood that a coal bed may also be referred to as a coal seam, or other deposit of coal that is accessible from surface, such as by a well drilled from surface. Furthermore, the hydrocarbons that may be produced form a coal bed are referred to herein as methane or coal bed methane, although the methane may also include a relatively small proportion of other, heavier hydrocarbons or other gases as is known in the art with respect to coalbed methane gas. In addition, the source of carbon dioxide is preferably a source of captured carbon dioxide, such as may be obtained from a power plant or other industrial activity. As it is primarily carbon dioxide that adsorbs to the coal and causes the methane to desorb, the source of carbon dioxide is preferably at least 90%
carbon dioxide gas, and preferably more, such as 95% or more. The actual composition of the source of carbon dioxide gas may vary depending on the source and any applicable regulations, but may also include other gases, such as oxygen, nitrogen, nitrogen-based gases, other carbon-based gases, etc.
carbon dioxide gas, and preferably more, such as 95% or more. The actual composition of the source of carbon dioxide gas may vary depending on the source and any applicable regulations, but may also include other gases, such as oxygen, nitrogen, nitrogen-based gases, other carbon-based gases, etc.
[0013] Coal can store two or more moles of carbon dioxide per mole of methane stored in coal. When carbon dioxide is adsorbed in coal, the methane stored in coal is desorbed and freed to be extracted and processed. The disclosed method provides an alternative solution to safely store carbon dioxide. For example, the Alberta Carbon Trunk Line to be commissioned in 2017 was built to collect and transport carbon dioxide produced in Alberta at major industrial sites for storage in deep saline aquifers and/or for use in EOR (enhanced oil recovery) operations. The 5 proposed method offers a different approach in a unique and innovative variant to store carbon dioxide that may become available from resources such as the Alberta Carbon Trunk Line and other sources of carbon dioxide. The system here described takes advantage of safely storing carbon dioxide in coal beds by an adsorption/desorption process that also produces methane stored in the same coal beds.
[0014] In 2016, Shell Canada commissioned Quest, a carbon capture and storage process where the carbon dioxide captured from its oil upgrading and refinery processes is compressed and stored in underground caverns. The Alberta Carbon Trunk Line is under construction and due to be commissioned in 2017. The objective of this line is to transport and distribute recovered carbon dioxide from Alberta facilities to store in deep saline aquifers and/or EOR
(Enhanced Oil Recovery) at oil wells. The use of carbon dioxide to enhance oil production is well documented and in operation since 2000 with success at Estevan, Saskatchewan. However, the use of carbon dioxide in EOR results in the continuous recycling and recompression of carbon dioxide into the oil formation. Historical records at Estevan showed that only 30 to 40%
of the carbon dioxide injected is stored under pressure in the oil reservoir, requiring a continuous recycling compression step.
(Enhanced Oil Recovery) at oil wells. The use of carbon dioxide to enhance oil production is well documented and in operation since 2000 with success at Estevan, Saskatchewan. However, the use of carbon dioxide in EOR results in the continuous recycling and recompression of carbon dioxide into the oil formation. Historical records at Estevan showed that only 30 to 40%
of the carbon dioxide injected is stored under pressure in the oil reservoir, requiring a continuous recycling compression step.
[0015] Coal beds have an affinity to absorb carbon dioxide and hence are an ideal storage resource. Furthermore, the injection of carbon dioxide into a coal bed can be used to establish an adsorption/desorption process that frees the methane and other volatile hydrocarbons stored in coal to be recovered, processed and distributed.
[0016] The method described herein provides a process that uses carbon dioxide that may be produced, recovered and transported for storage in coal fields and to extract stored methane and other volatile hydrocarbons from the coal beds. Carbon dioxide recovered from industrial activities and transported by, for example a pipeline such as the Alberta Carbon Trunk Line, may be injected into coal beds to enhance coal bed methane extraction while storing the carbon dioxide, unlike the pipeline proposed practice of compressing it into saline aquifers or oil wells.
Coal bed methane extraction works by replacing sorbed methane molecules with more strongly sorbed carbon dioxide molecules. The process is beneficial as coal selectivity of carbon dioxide to methane is greater than 2 to 1, coal adsorbs and stores 2 molecules or more of carbon dioxide for every molecule of methane displaced, and the carbon dioxide remains adsorbed in the coal and displaces the methane. The extracted methane may then be captured, processed and routed to natural gas pipeline distribution systems. The proposed method meets a need to first store carbon dioxide safely and secondly to recover coal stored methane gas and volatile hydrocarbons from a coal bed economically.
Coal bed methane extraction works by replacing sorbed methane molecules with more strongly sorbed carbon dioxide molecules. The process is beneficial as coal selectivity of carbon dioxide to methane is greater than 2 to 1, coal adsorbs and stores 2 molecules or more of carbon dioxide for every molecule of methane displaced, and the carbon dioxide remains adsorbed in the coal and displaces the methane. The extracted methane may then be captured, processed and routed to natural gas pipeline distribution systems. The proposed method meets a need to first store carbon dioxide safely and secondly to recover coal stored methane gas and volatile hydrocarbons from a coal bed economically.
[0017] The present method provides an alternative to store large volumes of recovered carbon dioxide safely, such as may be delivered by Alberta Carbon Trunk Line or other sources of carbon dioxide, and simultaneously extract methane from the coal beds for distribution. The description of application of the method herein should, therefore, be considered as an example.
[0018] FIG. 1 depicts a preferred method of storing carbon dioxide produced, recovered and transported by a resource such as the Alberta Carbon Trunk Line from industrial plants in Alberta.
[0019] Carbon dioxide is transported and distributed by Alberta Carbon Trunk Line through stream 1 into a coal bed site and further compressed by compressor 2 to meet optimum pressure conditions. The pressurized carbon dioxide stream 3 flows through a fin fan heat exchanger 4 to meet coal bed optimum temperature conditions for adsorption of carbon dioxide and desorption of methane stored in coal bed. The pressure and temperature controlled carbon dioxide stream 5 is injected into well 6 and distributed through slots 7 into the coal bed 8.
The injected pressure and temperature controlled carbon dioxide stream is adsorbed in coal bed 8 and the &sorbed methane and other volatile hydrocarbon gases are displaced across the coal bed 8 and through slots 9 into production well 10. The extracted methane is routed through production well 10 and through stream 11 into gas processing unit 12. The processed gas exits gas processing unit 12 through stream 13 to gas pipeline for distribution.
The injected pressure and temperature controlled carbon dioxide stream is adsorbed in coal bed 8 and the &sorbed methane and other volatile hydrocarbon gases are displaced across the coal bed 8 and through slots 9 into production well 10. The extracted methane is routed through production well 10 and through stream 11 into gas processing unit 12. The processed gas exits gas processing unit 12 through stream 13 to gas pipeline for distribution.
[0020] As noted, prior to injecting the carbon dioxide into the coal bed 8, it is conditioned through compression and temperature control. This is preferably done to achieve an optimal amount of carbon dioxide adsorption, which will in turn enhance methane production. The optimal temperature and pressure conditions may be selected by analysing the coal formation, or through experimentation. Optimization may also include an analysis of the energy required to condition the carbon dioxide and any effect the compression and temperature control has on downstream transport or processing.
[0021] In one example, the process may be implemented by: first, storing carbon dioxide delivered from the Alberta Carbon Trunk Line by adsorption in a coal bed;
second, desorbing and extracting stored methane from the coal bed; and third, processing and distributing the extracted coal bed methane. This process allows an efficient use of an abundant supply of recovered carbon dioxide for safe storage and simultaneous extraction of stored methane from the coal bed by establishing an adsorption/desorption process where carbon dioxide displaces and frees methane stored in a coal bed to flow into a production well. This process provides for coal beds to be a safe storage resource for carbon dioxide and to recover a clean source of energy from coal in the form of methane.
second, desorbing and extracting stored methane from the coal bed; and third, processing and distributing the extracted coal bed methane. This process allows an efficient use of an abundant supply of recovered carbon dioxide for safe storage and simultaneous extraction of stored methane from the coal bed by establishing an adsorption/desorption process where carbon dioxide displaces and frees methane stored in a coal bed to flow into a production well. This process provides for coal beds to be a safe storage resource for carbon dioxide and to recover a clean source of energy from coal in the form of methane.
[0022] In this patent document, the word "comprising" is used in its non-limiting sense to mean that items following the word are included, but items not specifically mentioned are not excluded. A reference to an element by the indefinite article "a" does not exclude the possibility that more than one of the element is present, unless the context clearly requires that there be one and only one of the elements.
[0023] The scope of the claims should not be limited by the preferred embodiments set forth in the examples, but should be given a broad purposive interpretation consistent with the description as a whole.
Claims (9)
1. A method to store carbon dioxide in a coal bed by desorption to coal in the coal bed, and to desorb, displace and extract methane stored in the coal bed, the method comprising the steps of:
providing a supply of carbon dioxide from a source of carbon dioxide to a coal bed site for storage;
providing a compressor to condition the pressure of the carbon dioxide;
providing an air heat exchanger to condition the temperature of the carbon dioxide;
providing an injection well to deliver the pressure and temperature conditioned carbon dioxide stream to the coal bed;
providing slots in an injection well to distribute the carbon dioxide into the coal bed;
providing slots in a coal bed production well to extract methane desorbed from the coal bed; and delivering the extracted methane to a gas processing unit.
providing a supply of carbon dioxide from a source of carbon dioxide to a coal bed site for storage;
providing a compressor to condition the pressure of the carbon dioxide;
providing an air heat exchanger to condition the temperature of the carbon dioxide;
providing an injection well to deliver the pressure and temperature conditioned carbon dioxide stream to the coal bed;
providing slots in an injection well to distribute the carbon dioxide into the coal bed;
providing slots in a coal bed production well to extract methane desorbed from the coal bed; and delivering the extracted methane to a gas processing unit.
2. The method of Claim 1, where the source of carbon dioxide is a pipeline that transports carbon dioxide under pressure.
3. The method of Claim 1, where the source of carbon dioxide comprises at least 90%
carbon dioxide gas.
carbon dioxide gas.
4. The method of Claim 1, where the pressure and temperature of the carbon dioxide is selected to be optimized for adsorption to coal in the coal bed.
5. The method of Claim 1, where the extracted methane is extracted and processed for distribution.
6. A method of carbon capture and methane production, comprising the steps of:
obtaining a source of pressurized carbon dioxide gas;
conditioning the carbon dioxide gas to achieve a desired pressure and temperature range;
injecting the conditioned carbon dioxide gas into a coal bed such that the carbon dioxide gas adsorbs to coal in the coal bed and desorbs methane from the coal;
and capturing the desorbed methane for transport or processing.
obtaining a source of pressurized carbon dioxide gas;
conditioning the carbon dioxide gas to achieve a desired pressure and temperature range;
injecting the conditioned carbon dioxide gas into a coal bed such that the carbon dioxide gas adsorbs to coal in the coal bed and desorbs methane from the coal;
and capturing the desorbed methane for transport or processing.
7. The method of claim 6, wherein the source of pressurized carbon dioxide gas is a pipeline.
8. The method of claim 6, wherein the source of pressurized carbon dioxide gas comprises at least 90% carbon dioxide.
9. The method of claim 6, wherein the carbon dioxide gas is conditioned to achieve optimized conditions for adsorption to the coal.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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CA2960997A CA2960997A1 (en) | 2017-03-16 | 2017-03-16 | Coal bed methane extraction and carbon capture |
CA2962169A CA2962169A1 (en) | 2017-03-16 | 2017-03-28 | Coal bed methane extraction and carbon capture |
PCT/CA2018/050293 WO2018165747A1 (en) | 2017-03-16 | 2018-03-12 | Coal bed methane extraction and carbon capture |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2960997A CA2960997A1 (en) | 2017-03-16 | 2017-03-16 | Coal bed methane extraction and carbon capture |
Publications (1)
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112160738A (en) * | 2020-09-18 | 2021-01-01 | 西安交通大学 | Well arrangement structure for underground in-situ pyrolysis of coal and construction method thereof |
CN114293962A (en) * | 2021-12-30 | 2022-04-08 | 中国矿业大学 | Closed-loop system for permeability increase of gas extraction utilization and reinjection coal seam and working method |
CN117211747A (en) * | 2023-09-28 | 2023-12-12 | 中国矿业大学 | Adsorption and concentration of CO in flue gas by coal seam 2 Zero-carbon co-mining method for coal and gas |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110652847B (en) * | 2019-11-14 | 2024-01-19 | 河南理工大学 | Device and method for disposing carbon dioxide in industrial waste gas based on coal mine goaf |
-
2017
- 2017-03-16 CA CA2960997A patent/CA2960997A1/en not_active Abandoned
- 2017-03-28 CA CA2962169A patent/CA2962169A1/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112160738A (en) * | 2020-09-18 | 2021-01-01 | 西安交通大学 | Well arrangement structure for underground in-situ pyrolysis of coal and construction method thereof |
CN114293962A (en) * | 2021-12-30 | 2022-04-08 | 中国矿业大学 | Closed-loop system for permeability increase of gas extraction utilization and reinjection coal seam and working method |
CN117211747A (en) * | 2023-09-28 | 2023-12-12 | 中国矿业大学 | Adsorption and concentration of CO in flue gas by coal seam 2 Zero-carbon co-mining method for coal and gas |
CN117211747B (en) * | 2023-09-28 | 2024-01-23 | 中国矿业大学 | Adsorption and concentration of CO in flue gas by coal seam 2 Zero-carbon co-mining method for coal and gas |
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