WO2013026421A1 - Underground coal gasification method - Google Patents
Underground coal gasification method Download PDFInfo
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- WO2013026421A1 WO2013026421A1 PCT/CN2012/082067 CN2012082067W WO2013026421A1 WO 2013026421 A1 WO2013026421 A1 WO 2013026421A1 CN 2012082067 W CN2012082067 W CN 2012082067W WO 2013026421 A1 WO2013026421 A1 WO 2013026421A1
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- gasification
- injection well
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- 238000002309 gasification Methods 0.000 title claims abstract description 84
- 239000003245 coal Substances 0.000 title claims abstract description 64
- 238000000034 method Methods 0.000 title claims abstract description 43
- 238000002347 injection Methods 0.000 claims abstract description 83
- 239000007924 injection Substances 0.000 claims abstract description 83
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000003054 catalyst Substances 0.000 claims abstract description 19
- 239000002245 particle Substances 0.000 claims abstract description 18
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 14
- 238000006243 chemical reaction Methods 0.000 claims abstract description 9
- 238000002485 combustion reaction Methods 0.000 claims abstract description 8
- 229910052751 metal Inorganic materials 0.000 claims abstract description 8
- 239000002184 metal Substances 0.000 claims abstract description 8
- 239000012530 fluid Substances 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 claims description 70
- 238000004519 manufacturing process Methods 0.000 claims description 34
- 238000005065 mining Methods 0.000 claims description 9
- 238000011084 recovery Methods 0.000 claims description 8
- 238000005553 drilling Methods 0.000 claims description 7
- 238000002955 isolation Methods 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- 238000005336 cracking Methods 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 4
- 239000011707 mineral Substances 0.000 abstract description 4
- 238000004891 communication Methods 0.000 abstract description 2
- 238000002407 reforming Methods 0.000 abstract 2
- 230000004931 aggregating effect Effects 0.000 abstract 1
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 238000012423 maintenance Methods 0.000 abstract 1
- 230000008569 process Effects 0.000 description 10
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- 238000005516 engineering process Methods 0.000 description 7
- 230000009466 transformation Effects 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 208000010392 Bone Fractures Diseases 0.000 description 3
- 206010017076 Fracture Diseases 0.000 description 3
- 239000003034 coal gas Substances 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000035515 penetration Effects 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 150000001340 alkali metals Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
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- 230000007774 longterm Effects 0.000 description 2
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- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
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- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
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- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- JVUDZIJPOLLFOJ-UHFFFAOYSA-K lithium potassium sodium carbonic acid hydrogen carbonate carbonate Chemical compound [Li+].[Na+].[K+].OC(O)=O.OC([O-])=O.[O-]C([O-])=O JVUDZIJPOLLFOJ-UHFFFAOYSA-K 0.000 description 1
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- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- AKEKKCGPLHMFCI-UHFFFAOYSA-L potassium sodium hydrogen carbonate Chemical compound [Na+].[K+].OC([O-])=O.OC([O-])=O AKEKKCGPLHMFCI-UHFFFAOYSA-L 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
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- 231100000331 toxic Toxicity 0.000 description 1
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- 239000002699 waste material Substances 0.000 description 1
Images
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
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/17—Interconnecting two or more wells by fracturing or otherwise attacking the formation
-
- 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
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
- E21B43/267—Methods for stimulating production by forming crevices or fractures reinforcing fractures by propping
-
- 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
Definitions
- the invention relates to a method for gasification of underground coal, in particular to a gasification method of a coal seam located at a depth of 500 meters to several kilometers below ground.
- Underground coal gasification is a kind of energy collection method that directly controls the underground coal to be controlled to burn, and the crude syngas is output to the ground through the thermal action and chemical action of coal. It is a well-built well, coal mining and conversion process. As one of the coal development technologies, it is especially suitable for coal seams that cannot be mined or uneconomically produced by conventional methods, and secondary or multiple recovery of coal mines.
- the underground coal gasification process requires that the coal seam has a strong gas permeability.
- the natural permeability of the coal seam is very poor, so it is necessary to pass through the gasification passage in the coal seam before the underground coal gasification operation.
- the direction of the connection between the well and the gasifier injection well is used as the direction of the gasification passage.
- At least three wells must be drilled by this method to roughly determine the gasification channel, and the cost is high.
- the gasification channel determined by this method is inefficient, and there is often a gasification channel that cannot be selected, and the gasification channel needs to be re-determined. The case of going through again.
- a method and system for determining and penetrating underground coal gasification passages comprising: measuring the coal seam level Ground stress in the direction; determining the development direction of the coal seam crack according to the ground stress in the horizontal direction; determining the direction of the coal gasification channel according to the development direction of the coal seam crack.
- the defect of this method is to improve the underground gasification and penetration efficiency and save the penetration time. It is also necessary to install the underground gasification passage through device described in CN201802362U, and the gasification reaction area is small and the gasification efficiency is low.
- a gasification pilot test gasification furnace for underground coal and a process method thereof comprising the gas supply system, the gasification furnace, the temperature measurement and pressure measurement component system, the high temperature camera system, the gas purification system.
- the gasifier shell is lined with refractory material. The gasifier and process are only suitable for use in the original coal mine roadway and cannot be used in coal seams located at a depth of 500m or even 2000m below the surface.
- the coal gas is first converted into products such as hydrogen and carbon monoxide, and then the synthesis gas is synthesized into methane under the action of a catalyst.
- catalysts are alkali metal catalysts, such as potassium carbonate, sodium carbonate, or polybasic alkali metal composite catalysts, such as potassium carbonate-sodium carbonate binary catalyst or potassium carbonate-sodium carbonate-lithium carbonate ternary catalyst.
- alkali metal catalysts such as potassium carbonate, sodium carbonate, or polybasic alkali metal composite catalysts, such as potassium carbonate-sodium carbonate binary catalyst or potassium carbonate-sodium carbonate-lithium carbonate ternary catalyst.
- the present invention provides a method for underground coal gasification, in particular, a gasification method for a coal seam located at a depth of less than 500 m underground.
- the method includes:
- the above gasification operation area may be more than 0.5 square kilometers, and an isolation area may be provided between the gasification operation areas; the separation area is more than 500 meters;
- the distance between the injection well and the gas production well is between 150 meters and 500 meters.
- the injection wells and gas production wells can be set up using the original well network to carry out underground coal gasification operations.
- the above-mentioned gasification channel uses a fracturing device to fracturing the coal seam, and injects a fluid medium into the injection well and the gas production well to add a catalyst and a proppant, and the injection pressure is greater than the fracture pressure of the formation to form a large
- Smaller particles of catalyst and proppant may be injected into the cracks described above, such as particles having a diameter of 1-2 mm, in which larger particles of catalyst and proppant are injected into the gasification passage, such as particles having a diameter of 10-20 mm.
- the above catalyst and proppant may be a substance such as metal ore particles, and it is preferred to select lower cost iron ore particles.
- the metal ore particles have both a catalytic action and a support for the gasification passage.
- the above injection wells can be divided into gas injection wells, water injection wells, and water injection wells located between the gas injection wells and the gas production wells.
- the above gasifying agent may be air or oxygen.
- the above-mentioned gas injection wells, water injection wells and gas production wells can be arranged in a square queue, and the gas injection wells at the edge are arranged in sequence.
- the injection well and the gas production well are gradually advanced with the combustion zone advancement. Converted to gas injection wells and water injection wells.
- gas injection wells, water injection wells and gas production wells may be arranged in queues of other shapes, such as plum-shaped piles, rings, and the like.
- the invention adopts a relatively closed underground coal seam as a whole gasification reaction vessel, and utilizes drilling engineering technology and new directional drilling, fracturing transformation and other engineering techniques as a coal seam transformation, injection and matching supporting technology, and changes the existing technology to a small area.
- the shortcomings of low displacement efficiency reflect the characteristics of mining technology with large area, high efficiency and high calorific value, so as to achieve efficient and comprehensive development of coal resources.
- the specific advantages are as follows:
- the invention adopts large-scale fracturing transformation to form primary and secondary fracture channels, and directional injection channels formed by directional drilling, that is, combined with the fluid medium, fracturing, orientation and other harvesting technologies used in the development of the mine field. It will form the largest ripple effect and displacement effect, which can transform coal resources to the greatest extent and avoid waste of resources.
- the invention adopts the method of injecting water and oxygen in the underground coal seam, and the high-efficiency injection-production connecting well network utilized, and the coal-fired gas produced under the action of high temperature and high pressure is higher than the prior art.
- the combustion value has been greatly increased, which has played a good role in energy conservation and consumption reduction for resource utilization and downstream production.
- the coal fracture cracking transformation utilizes the inter-well crack channel formed by the large-scale fracturing transformation, and the metal mineral particles are used as the inter-well channel proppant, which can effectively maintain the long-term effective communication between the injection-production well networks, and the long-term large-area Scale mining plays a good production base; and metal mineral particles can play a catalytic polymerization role in the gasification process, which has a significant effect on increasing coal gas production.
- the invention adopts a gasification channel as a gasification reaction zone, omitting a special gasifier equipment, and saving cost;
- the invention separately injects a gasification agent and a water injection well by separately injecting a gasification agent and water, which is beneficial to the gasification reaction of the coal seam;
- the invention has an isolation zone between the gasification operation zones, which effectively prevents the surface from collapsing due to gasification operations.
- Figure 1 is a schematic view of a gasification working area and an isolation area of the present invention
- FIG. 2 is a schematic view showing the distribution mode 1 of the injection well and the gas production well in the gasification operation area of the present invention
- FIG. 3 is a schematic view showing the distribution mode 2 of the injection well and the gas production well in the gasification operation area of the present invention
- FIG. 4 is a schematic view showing the distribution mode 3 of the injection well and the gas production well in the gasification operation area of the present invention
- Figure 5 is a schematic view of the gas injection well injection device of the present invention.
- Figure 6 is a schematic view of the water injection well injection device of the present invention.
- Figure 7 is a schematic view of a gasification passage between an injection well and a gas production well according to the present invention.
- Figure 8 is a schematic view of the gas recovery well recovery device of the present invention.
- Figure 9 is a flow chart of the ground recycling process of the present invention.
- an isolation zone (2) is provided between the gasification operation zones (1) of the present invention, and an injection well (3) and a gas production well (4) are provided in the gasification operation zone.
- the width of the isolation zone is above 500m.
- the injection well (3) of the present invention can be divided into a gas injection well (5) and a water injection well (6), respectively, and the water injection well (6) is located in the gas injection well (5) and the gas production well (4). between.
- the gas injection well (5), the water injection well (6) and the gas production well (4) may be arranged in a rectangular manner, and the gas injection well (5) located at the edge is arranged in sequence as a water injection well (6) and a gas production well (4), in the mining project.
- the injection well (6) and the gas production well (4) are gradually converted into a gas injection well (5) and a water injection well (6) as the combustion zone advances.
- the gas injection well (5), the water injection well (6) and the gas production well (4) may be arranged in a plum shape, ring shape or other manner.
- the gasifying agent of the present invention may be air or oxygen, which is passed through a gasifying agent gas injection line (7), a nozzle (8), and a casing (9) on the gas injection well (5).
- a gasification agent injection device composed of a tubing (10), a packer (11), a valve (12), and a single flow valve (13) is injected into the coal seam.
- the present invention injects water into and near the coal seam combustion zone through a water injection device consisting of a casing (14), a fuel pipe (15), a valve (16), and a check valve (17).
- a gasification passage is provided between the injection well and the gas production well of the present invention.
- the gas produced by the present invention is recovered by a recovery unit consisting of a casing (18), a fuel pipe (19), a valve (20) and a check valve (21).
- the ground recycling treatment process of the present invention comprises underground mixing of a mixed fluid, separating gases, liquids and solids by means of three separation devices, and further processing by a water treatment device, a desulfurization and dust removal device, and the like.
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- Mining & Mineral Resources (AREA)
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- Environmental & Geological Engineering (AREA)
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Abstract
An underground coal gasification method. The method comprises disposing multiple injection wells (3) and gas collection wells (4) in a gasification operation zone; adding a catalyst and a propping agent into injection wells and gas collection wells by means of a fluid medium; fracturing and reforming the coal layer using a fracturing device to form large areas of fissures and cracks; forming gasification paths in the form of directional wells between the injection wells and gas collection wells; adding a gasification agent, a catalyst, and water through the injection wells to cause coal layer combustions and chemical reactions; collecting at the gas collection wells the gas produced by means of collection devices. The fissure paths between the wells formed by reforming large fractures, and the metal mineral particles used as a propping agent for the paths between wells effectively enable the maintenance of the effective communication in the injection well network for long durations; the metal mineral particles also function as a catalyst and an aggregating agent during gasification, thereby substantially enhancing the coal gasification volume.
Description
技术领域Technical field
本发明涉及一种地下煤炭气化的方法,尤其是位于地下500米至数千米以下深度的煤层的气化方法。The invention relates to a method for gasification of underground coal, in particular to a gasification method of a coal seam located at a depth of 500 meters to several kilometers below ground.
背景技术Background technique
煤炭地下气化即直接将处于地下的煤炭进行有控制地燃烧,通过对煤的热作用及化学作用产生粗合成气后输出地面的一种能源采集方式,是集建井、采煤、转化工艺为一体的煤炭开发技术,特别适用于常规方法不可采或者开采不经济的煤层,以及煤矿的二次或者多次复采。Underground coal gasification is a kind of energy collection method that directly controls the underground coal to be controlled to burn, and the crude syngas is output to the ground through the thermal action and chemical action of coal. It is a well-built well, coal mining and conversion process. As one of the coal development technologies, it is especially suitable for coal seams that cannot be mined or uneconomically produced by conventional methods, and secondary or multiple recovery of coal mines.
煤炭地下气化工艺要求煤层具有较强的气体渗透能力。然而煤层的天然渗透能力很差,因此在进行煤炭地下气化操作之前需要先在煤层之中贯通气化通道。通常做法是在气化剂注入井周围几个不同方向分别打井,之后向气化剂注入井注入高压气体,观察气化剂注入井周围的几口井中排除气体的量,选择排气量最大的井与气化剂注入井的连线方向作为气化通道方向。利用此方法至少要钻三口井,才能大致确定气化通道,成本较高,此外,此方法确定的气化通道效率较低,经常会出现无法贯通选择的气化通道、需要重新确定气化通道再次进行贯通的情况。The underground coal gasification process requires that the coal seam has a strong gas permeability. However, the natural permeability of the coal seam is very poor, so it is necessary to pass through the gasification passage in the coal seam before the underground coal gasification operation. It is common practice to drill wells in several different directions around the gasifier injection well, then inject high pressure gas into the gasification injection well, observe the amount of gas removed from several wells around the gasification injection well, and select the largest exhaust gas. The direction of the connection between the well and the gasifier injection well is used as the direction of the gasification passage. At least three wells must be drilled by this method to roughly determine the gasification channel, and the cost is high. In addition, the gasification channel determined by this method is inefficient, and there is often a gasification channel that cannot be selected, and the gasification channel needs to be re-determined. The case of going through again.
针对上述存在的确定、贯通气化通道的方法成本较高,贯通效率较低的问题,在CN1014241181A中,公开了一种煤炭地下气化通道确定、贯通方法和系统,其方法包括:测量煤层水平方向的地应力;根据测量水平方向的地应力,确定所述煤层裂隙发育方向;根据所述煤层裂隙发育方向确定所述煤炭气化通道的方向。该方法的缺陷是要提高地下气化贯通效率,节约贯通时间,还需专门安装CN201802362U所述的地下气化通道贯通装置,并且,该方法气化反应面积小,气化效率低。In view of the above-mentioned problem of determining the cost of passing through the gasification passage and the low penetration efficiency, in CN1014241181A, a method and system for determining and penetrating underground coal gasification passages are disclosed, the method comprising: measuring the coal seam level Ground stress in the direction; determining the development direction of the coal seam crack according to the ground stress in the horizontal direction; determining the direction of the coal gasification channel according to the development direction of the coal seam crack. The defect of this method is to improve the underground gasification and penetration efficiency and save the penetration time. It is also necessary to install the underground gasification passage through device described in CN201802362U, and the gasification reaction area is small and the gasification efficiency is low.
在CN101586915B中,公开了一种地下煤的气化中试试验气化炉及其工艺方法,其方法包括气体供应系统、气化炉、测温测压测组分系统、高温摄像系统、煤气净化系统。气化炉外壳内衬有耐火材料。该气化炉及工艺仅适于在原煤矿巷道内使用,无法在位于地表下500m,甚至2000m深度的煤层使用。In CN101586915B, a gasification pilot test gasification furnace for underground coal and a process method thereof are disclosed, the method comprising the gas supply system, the gasification furnace, the temperature measurement and pressure measurement component system, the high temperature camera system, the gas purification system. The gasifier shell is lined with refractory material. The gasifier and process are only suitable for use in the original coal mine roadway and cannot be used in coal seams located at a depth of 500m or even 2000m below the surface.
在煤炭地下气化过程中,先将煤气化成氢气和一氧化碳等产品,然后再将合成气在催化剂作用下合成甲烷。通常选用的催化剂大多为碱金属催化剂,如碳酸钾、碳酸钠,或者多元碱金属复合催化剂,如碳酸钾-碳酸钠二元催化剂或者碳酸钾-碳酸钠-碳酸锂三元催化剂,上述催化剂存在使用量大、成本高,还需安装回收装置进行回收等问题。In the underground coal gasification process, the coal gas is first converted into products such as hydrogen and carbon monoxide, and then the synthesis gas is synthesized into methane under the action of a catalyst. Most commonly used catalysts are alkali metal catalysts, such as potassium carbonate, sodium carbonate, or polybasic alkali metal composite catalysts, such as potassium carbonate-sodium carbonate binary catalyst or potassium carbonate-sodium carbonate-lithium carbonate ternary catalyst. Large quantities, high cost, and the need to install recycling equipment for recycling and other issues.
发明内容Summary of the invention
为克服现有技术之不足,本发明提供一种地下煤炭气化的方法,尤其是位于地下500m以下深度的煤层的气化方法。该方法包括:In order to overcome the deficiencies of the prior art, the present invention provides a method for underground coal gasification, in particular, a gasification method for a coal seam located at a depth of less than 500 m underground. The method includes:
1、根据勘测结果,确定气化作业区;1. Determine the gasification operation area according to the survey results;
2、在气化作业区设置若干个注入井和采气井;2. Set up several injection wells and gas production wells in the gasification operation area;
3、在注入井和采气井之间以定向井(可以为水平井,也可以为倾斜井)的方式形成气化通道;3. Forming a gasification channel between the injection well and the gas production well by means of a directional well (which may be a horizontal well or a inclined well);
4、通过注入井注入气化剂、催化剂及水,促使煤层燃烧并进行化学反应;4. Injecting a gasifying agent, a catalyst and water through the injection well to promote combustion of the coal seam and carry out a chemical reaction;
5、通过回收装置在采气井回收所产生气体。5. Recover the generated gas in the gas recovery well through the recovery unit.
上述的气化作业区面积可以在0.5平方千米以上,气化作业区之间可以设有隔离区;隔离区间隔为500米以上;The above gasification operation area may be more than 0.5 square kilometers, and an isolation area may be provided between the gasification operation areas; the separation area is more than 500 meters;
上述注入井和采气井之间的距离在150米—500米之间。当煤层气田开采后,注入井和采气井可以利用原有井网设置,实施地下煤炭气化作业。The distance between the injection well and the gas production well is between 150 meters and 500 meters. After the coalbed methane field is mined, the injection wells and gas production wells can be set up using the original well network to carry out underground coal gasification operations.
上述的气化通道在定向钻井前,利用压裂装置对煤层进行压裂改造,向注入井和采气井中注入流体介质加入催化剂和支撑剂,注入压力大于地层的破裂压力即可,以形成大面积裂隙裂缝,与此后通过定向钻井形成的气化通道共同构成气化通道体系。Before the directional drilling, the above-mentioned gasification channel uses a fracturing device to fracturing the coal seam, and injects a fluid medium into the injection well and the gas production well to add a catalyst and a proppant, and the injection pressure is greater than the fracture pressure of the formation to form a large The area cracks, together with the gasification channels formed by directional drilling, constitute a gasification channel system.
在上述的裂隙裂缝中可以注入较小颗粒的催化剂和支撑剂,如颗粒直径为1-2mm,在气化通道内注入较大颗粒的催化剂和支撑剂,如颗粒直径为10-20mm。Smaller particles of catalyst and proppant may be injected into the cracks described above, such as particles having a diameter of 1-2 mm, in which larger particles of catalyst and proppant are injected into the gasification passage, such as particles having a diameter of 10-20 mm.
上述的催化剂和支撑剂可以为一种物质,如金属矿石颗粒,最好选择成本较低的铁矿石颗粒。该金属矿石颗粒既有催化剂作用,还有支撑气化通道的作用。The above catalyst and proppant may be a substance such as metal ore particles, and it is preferred to select lower cost iron ore particles. The metal ore particles have both a catalytic action and a support for the gasification passage.
上述的注入井可以分设,分别为注气井,注水井,注水井位于注气井和采气井之间。The above injection wells can be divided into gas injection wells, water injection wells, and water injection wells located between the gas injection wells and the gas production wells.
上述的气化剂可以为空气,也可以为氧气。The above gasifying agent may be air or oxygen.
上述的注气井、注水井和采气井可以排列为方形队列,位于边缘的为注气井,依次排列,在开采工程中,初期的注气井燃烧后,随着燃烧区推进,注水井和采气井逐步转换为注气井和注水井。The above-mentioned gas injection wells, water injection wells and gas production wells can be arranged in a square queue, and the gas injection wells at the edge are arranged in sequence. In the mining project, after the initial gas injection well is burned, the injection well and the gas production well are gradually advanced with the combustion zone advancement. Converted to gas injection wells and water injection wells.
上述的注气井、注水井和采气井可以排列为其他形状的队列,如梅花桩形,环形等。The above-mentioned gas injection wells, water injection wells and gas production wells may be arranged in queues of other shapes, such as plum-shaped piles, rings, and the like.
对于多煤层的矿区最好采取先开采底层煤层,然后,依次向上层推进的方式开采。For the mining area with multiple coal seams, it is best to first mine the bottom coal seam and then, in turn, to the upper layer for mining.
本发明是将相对封闭的地下煤层作为一个整体气化反应容器,利用钻井工程技术以及新型定向钻井、压裂改造等工程技术作为煤层改造、注采配套工艺技术,改变现有技术波及面积小、驱替效率不高的缺点,体现大面积、高效率、高热值的开采工艺技术特点,从而达到煤资源的高效综合开发。具体优点如下:The invention adopts a relatively closed underground coal seam as a whole gasification reaction vessel, and utilizes drilling engineering technology and new directional drilling, fracturing transformation and other engineering techniques as a coal seam transformation, injection and matching supporting technology, and changes the existing technology to a small area. The shortcomings of low displacement efficiency reflect the characteristics of mining technology with large area, high efficiency and high calorific value, so as to achieve efficient and comprehensive development of coal resources. The specific advantages are as follows:
1、本项专利技术煤制气转化工艺流程均在地下完成,不会造成如传统工艺在地面生产形成的粉尘、有毒有害气体产生的环境污染。1. The patented technology coal gas conversion process is completed underground, and will not cause environmental pollution caused by dust and toxic and harmful gases formed by traditional processes on the ground.
2、可对埋藏较深(500-数千米)难以开采利用的煤炭资源进行开发,使得难动用煤炭资源开发得到有效实施,对今后此类煤资源综合开发起到示范效应。2. It is possible to develop coal resources that are difficult to exploit and use in deep burial (500-kilometres), so that the development of difficult-to-use coal resources can be effectively implemented, which will play a demonstration role in the comprehensive development of such coal resources in the future.
3、本发明采用大型压裂改造形成主次裂缝通道,以及利用定向钻井形成的定向注入通道,即结合矿场开发过程中所采用的注入驱替用流体介质、压裂、定向等采收技术,形成最大的波及效应和驱替效果,能最大程度的转化煤资源,避免资源浪费。3. The invention adopts large-scale fracturing transformation to form primary and secondary fracture channels, and directional injection channels formed by directional drilling, that is, combined with the fluid medium, fracturing, orientation and other harvesting technologies used in the development of the mine field. It will form the largest ripple effect and displacement effect, which can transform coal resources to the greatest extent and avoid waste of resources.
4、本发明由于采用在地下煤层中注入水、氧气交替还原反应,以及所利用的高效注采连通井网,在高温高压环境作用下,所采出的煤制气较现有技术其产量和燃烧值均有较大增加,对资源利用、下游生产均起到良好的节能降耗作用。4. The invention adopts the method of injecting water and oxygen in the underground coal seam, and the high-efficiency injection-production connecting well network utilized, and the coal-fired gas produced under the action of high temperature and high pressure is higher than the prior art. The combustion value has been greatly increased, which has played a good role in energy conservation and consumption reduction for resource utilization and downstream production.
5、本发明中煤层压裂改造利用大型压裂改造形成的井间裂缝通道,采用金属矿物颗粒作为井间通道支撑剂,可有效保持注采井网间的长时间有效连通,对于长期大面积规模开采起到良好的生产基础;且金属矿物颗粒能在气化过程中发挥催化聚合作用,对于提高煤制气产量具有显著的效果。5. In the invention, the coal fracture cracking transformation utilizes the inter-well crack channel formed by the large-scale fracturing transformation, and the metal mineral particles are used as the inter-well channel proppant, which can effectively maintain the long-term effective communication between the injection-production well networks, and the long-term large-area Scale mining plays a good production base; and metal mineral particles can play a catalytic polymerization role in the gasification process, which has a significant effect on increasing coal gas production.
6、本发明以气化通道作为气化反应区,省略了专门的气化炉设备,节约了成本;6. The invention adopts a gasification channel as a gasification reaction zone, omitting a special gasifier equipment, and saving cost;
7、本发明通过分设注气井和注水井,分别注入气化剂和水,有利于煤层气化反应;7. The invention separately injects a gasification agent and a water injection well by separately injecting a gasification agent and water, which is beneficial to the gasification reaction of the coal seam;
8、本发明在气化作业区之间设有隔离区,有效防止了地表因气化作业而塌陷。8. The invention has an isolation zone between the gasification operation zones, which effectively prevents the surface from collapsing due to gasification operations.
附图说明DRAWINGS
图1为本发明气化作业区和隔离区的示意图;Figure 1 is a schematic view of a gasification working area and an isolation area of the present invention;
图2为本发明气化作业区内注入井和采气井的分布方式一的示意图2 is a schematic view showing the distribution mode 1 of the injection well and the gas production well in the gasification operation area of the present invention;
图3为本发明气化作业区内注入井和采气井的分布方式二的示意图3 is a schematic view showing the distribution mode 2 of the injection well and the gas production well in the gasification operation area of the present invention;
图4为本发明气化作业区内注入井和采气井的分布方式三的示意图4 is a schematic view showing the distribution mode 3 of the injection well and the gas production well in the gasification operation area of the present invention;
图5为本发明注气井注入装置的示意图;Figure 5 is a schematic view of the gas injection well injection device of the present invention;
图6为本发明注水井注入装置的示意图;Figure 6 is a schematic view of the water injection well injection device of the present invention;
图7为本发明注入井和采气井间气化通道示意图;Figure 7 is a schematic view of a gasification passage between an injection well and a gas production well according to the present invention;
图8为本发明采气井回收装置的示意图;Figure 8 is a schematic view of the gas recovery well recovery device of the present invention;
图9为本发明地面回收处理工艺流程图。Figure 9 is a flow chart of the ground recycling process of the present invention.
具体实施方式detailed description
以下结合附图对本发明的具体实施例做进一步详述。Specific embodiments of the present invention will be further described in detail below with reference to the accompanying drawings.
参照图1,本发明的气化作业区(1)之间设有隔离区(2),气化作业区内设有注入井(3)和采气井(4)。隔离区的宽度在500m以上。Referring to Fig. 1, an isolation zone (2) is provided between the gasification operation zones (1) of the present invention, and an injection well (3) and a gas production well (4) are provided in the gasification operation zone. The width of the isolation zone is above 500m.
参照图2至图4,本发明的注入井(3)可以分设,分别为注气井(5)和注水井(6),注水井(6)位于注气井(5)和采气井(4)之间。注气井(5)、注水井(6)和采气井(4)可以矩形方式排列,位于边缘的为注气井(5),依次排列为注水井(6)和采气井(4),在开采工程中,初期的注气井(5)燃烧后,随着燃烧区推进,注水井(6)和采气井(4)逐步转换为注气井(5)和注水井(6)。注气井(5)、注水井(6)和采气井(4)可以梅花桩形,环形或者其他方式排列。Referring to Figures 2 to 4, the injection well (3) of the present invention can be divided into a gas injection well (5) and a water injection well (6), respectively, and the water injection well (6) is located in the gas injection well (5) and the gas production well (4). between. The gas injection well (5), the water injection well (6) and the gas production well (4) may be arranged in a rectangular manner, and the gas injection well (5) located at the edge is arranged in sequence as a water injection well (6) and a gas production well (4), in the mining project. After the initial gas injection well (5) is burned, the injection well (6) and the gas production well (4) are gradually converted into a gas injection well (5) and a water injection well (6) as the combustion zone advances. The gas injection well (5), the water injection well (6) and the gas production well (4) may be arranged in a plum shape, ring shape or other manner.
参照图5,本发明气化剂可以是空气,也可以是氧气,系通过注气井(5)上的由气化剂注气管线(7)、防喷管(8)、套管(9)、油管(10)、封隔器(11)、阀门(12)以及单流阀(13)所组成的气化剂注入装置注入煤层。Referring to Fig. 5, the gasifying agent of the present invention may be air or oxygen, which is passed through a gasifying agent gas injection line (7), a nozzle (8), and a casing (9) on the gas injection well (5). A gasification agent injection device composed of a tubing (10), a packer (11), a valve (12), and a single flow valve (13) is injected into the coal seam.
参照图6,本发明通过由套管(14)、油管(15)、阀门(16)及单向阀(17)组成的注水装置将水注入到煤层燃烧区及其附近。Referring to Figure 6, the present invention injects water into and near the coal seam combustion zone through a water injection device consisting of a casing (14), a fuel pipe (15), a valve (16), and a check valve (17).
参照图7,本发明注入井和采气井间设有气化通道。Referring to Figure 7, a gasification passage is provided between the injection well and the gas production well of the present invention.
参照图8,本发明所产气体通过由套管(18)、油管(19)、阀门(20)及单向阀(21)组成的回收装置进行回收。Referring to Figure 8, the gas produced by the present invention is recovered by a recovery unit consisting of a casing (18), a fuel pipe (19), a valve (20) and a check valve (21).
参照图9,本发明地面回收处理工艺包括地下产出混合流体,通过三项分离装置分离气体、液体和固体,并经过水处理装置、脱硫除尘装置等进一步处理。Referring to Fig. 9, the ground recycling treatment process of the present invention comprises underground mixing of a mixed fluid, separating gases, liquids and solids by means of three separation devices, and further processing by a water treatment device, a desulfurization and dust removal device, and the like.
Claims (14)
1、一种地下煤炭气化的方法,包括在气化作业区设置若干个注入井和采气井,其特征在于: 1. A method of underground coal gasification comprising the provision of a plurality of injection wells and gas production wells in a gasification operation zone, characterized in that:
(1)在注入井和采气井之间以定向井的方式形成气化通道;(1) forming a gasification passage between the injection well and the gas production well by directional wells;
(2)通过注入井注入气化剂、催化剂及水,促使煤层燃烧并进行化学反应;(2) injecting a gasifying agent, a catalyst and water through the injection well to promote combustion of the coal seam and carry out a chemical reaction;
(3)通过回收装置在采气井回收所产气体。(3) Recovering the produced gas in the gas recovery well through the recovery unit.
2、如权利要求1所述的一种地下煤炭气化的方法,其特征在于上述的气化通道在定向钻井前,通过流体介质向注入井和采气井中加入催化剂和支撑剂,并利用压裂装置对煤层进行压裂改造,形成大面积裂隙裂缝,与此后通过定向钻井形成的气化通道共同构成气化通道体系。2. A method of underground coal gasification according to claim 1, wherein said gasification passage adds catalyst and proppant to the injection well and the gas production well through the fluid medium before directional drilling, and utilizes pressure. The cracking device transforms the coal seam to form a large-area crack crack, and then forms a gasification passage system by a gasification passage formed by directional drilling.
3、如权利要求1或者2所述的一种地下煤炭气化的方法,其特征在于在上述的裂隙裂缝中注入较小颗粒的催化剂和支撑剂,颗粒直径为1-2mm,在气化通道内注入较大颗粒的催化剂和支撑剂,颗粒直径为10-20mm。3. A method of underground coal gasification according to claim 1 or 2, wherein a smaller particle catalyst and proppant are injected into said fracture crack, the particle diameter is 1-2 mm, in the gasification passage. The catalyst and proppant are injected with larger particles, and the particle diameter is 10-20 mm.
4、如权利要求3所述的一种地下煤炭气化的方法,其特征在于上述的催化剂和支撑剂为金属矿石颗粒。4. A method of underground coal gasification as claimed in claim 3 wherein said catalyst and proppant are metal ore particles.
5、如权利要求4所述的一种地下煤炭气化的方法,其特征在于上述的金属矿石颗粒为铁矿石颗粒。5. A method of underground coal gasification as claimed in claim 4 wherein said metal ore particles are iron ore particles.
6、如权利要求1所述的一种地下煤炭气化的方法,其特征在于上述的气化作业区面积在0.5平方千米以上,气化作业区之间设有隔离区;隔离区宽度为500米以上。6. A method of underground coal gasification according to claim 1, wherein said gasification operation area has an area of more than 0.5 square kilometers, and an isolation area is provided between the gasification operation areas; More than 500 meters.
7、如权利要求1或者6所述的一种地下煤炭气化的方法,其特征在于上述注入井和采气井之间的距离在150米—500米之间。7. A method of underground coal gasification according to claim 1 or claim 6 wherein the distance between said injection well and the gas production well is between 150 and 500 meters.
8、如权利要求1所述的一种地下煤炭气化的方法,其特征在于上述的注入井分设为注气井和注水井,注水井位于注气井和采气井之间。8. A method of underground coal gasification according to claim 1, wherein said injection well is divided into a gas injection well and a water injection well, and the water injection well is located between the gas injection well and the gas production well.
9、如权利要求1或者8所述的一种地下煤炭气化的方法,其特征在于上述的气化剂为空气。 9. A method of underground coal gasification according to claim 1 or claim 8 wherein said gasifying agent is air.
10、如权利要求9所述的一种地下煤炭气化的方法,其特征在于上述气化剂为氧气。10. A method of underground coal gasification as claimed in claim 9 wherein said gasifying agent is oxygen.
11、如权利要求1所述的一种地下煤炭气化的方法,其特征在于上述的注气井、注水井和采气井以方形排列,位于边缘的为注气井,依次排列,在开采中,初期的注气井燃烧后,随着燃烧区推进,注水井和采气井逐步转换为注气井和注水井。11. A method of underground coal gasification according to claim 1, wherein said gas injection well, water injection well and gas production well are arranged in a square shape, and gas injection wells located at the edge are arranged in sequence, in the initial stage of mining. After the gas injection well is burned, the injection well and the gas production well are gradually converted into a gas injection well and a water injection well as the combustion zone advances.
12、如权利要求1所述的一种地下煤炭气化的方法,其特征在于上述的注气井、注水井和采气井以梅花桩形排列。12. A method of underground coal gasification according to claim 1, wherein said gas injection well, water injection well and gas production well are arranged in a plum pile shape.
13、如权利要求1所述的一种地下煤炭气化的方法,其特征在于上述的注气井、注水井和采气井以环形排列。13. A method of underground coal gasification according to claim 1 wherein said gas injection well, water injection well and gas production well are arranged in a ring.
14、如权利要求1所述的一种地下煤炭气化的方法,其特征在于多煤层开采从底层开始,依次向上层推进的方式开采。14. A method of underground coal gasification as claimed in claim 1 wherein the multi-coal mining begins at the bottom and is subsequently carried out in an upward propulsion manner.
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101113670A (en) * | 2007-09-04 | 2008-01-30 | 新奥能源研究院有限公司 | Coal underground gasifying technology |
CN101113671A (en) * | 2007-09-04 | 2008-01-30 | 新奥能源研究院有限公司 | Underground catalytic gasification process of coal |
CN101424181A (en) | 2008-12-05 | 2009-05-06 | 新奥科技发展有限公司 | Method and system for determining and penetrating underground coal gasification passage |
RU2396305C1 (en) * | 2008-04-02 | 2010-08-10 | Общество с ограниченной ответственностью "Научно-производственная фирма "Медведь" | Method of hydrogen formation from coal-bearing layer |
RU2402595C2 (en) * | 2007-11-28 | 2010-10-27 | Общество с ограниченной ответственностью "Научно-производственная фирма "Медведь" | Cyclic procedure of carbon underground gasification |
CN101586915B (en) | 2009-04-29 | 2010-12-08 | 新奥科技发展有限公司 | Gasification furnace for the gasification pilot plant test of underground coal and process thereof |
CN201802362U (en) | 2010-08-02 | 2011-04-20 | 新奥科技发展有限公司 | Underground gasification passage through device |
CN102287177A (en) * | 2011-08-19 | 2011-12-21 | 秦勇 | Method for gasifying underground coal |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101315026B (en) * | 2008-07-01 | 2011-08-31 | 北京中矿科能煤炭地下气化技术研究中心 | Underground coal gasification system and producing process |
-
2011
- 2011-08-19 CN CN2011102558358A patent/CN102287177A/en active Pending
-
2012
- 2012-09-26 EA EA201400149A patent/EA201400149A1/en unknown
- 2012-09-26 EP EP12825017.2A patent/EP2843185A1/en not_active Withdrawn
- 2012-09-26 WO PCT/CN2012/082067 patent/WO2013026421A1/en active Application Filing
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101113670A (en) * | 2007-09-04 | 2008-01-30 | 新奥能源研究院有限公司 | Coal underground gasifying technology |
CN101113671A (en) * | 2007-09-04 | 2008-01-30 | 新奥能源研究院有限公司 | Underground catalytic gasification process of coal |
RU2402595C2 (en) * | 2007-11-28 | 2010-10-27 | Общество с ограниченной ответственностью "Научно-производственная фирма "Медведь" | Cyclic procedure of carbon underground gasification |
RU2396305C1 (en) * | 2008-04-02 | 2010-08-10 | Общество с ограниченной ответственностью "Научно-производственная фирма "Медведь" | Method of hydrogen formation from coal-bearing layer |
CN101424181A (en) | 2008-12-05 | 2009-05-06 | 新奥科技发展有限公司 | Method and system for determining and penetrating underground coal gasification passage |
CN101586915B (en) | 2009-04-29 | 2010-12-08 | 新奥科技发展有限公司 | Gasification furnace for the gasification pilot plant test of underground coal and process thereof |
CN201802362U (en) | 2010-08-02 | 2011-04-20 | 新奥科技发展有限公司 | Underground gasification passage through device |
CN102287177A (en) * | 2011-08-19 | 2011-12-21 | 秦勇 | Method for gasifying underground coal |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112012714A (en) * | 2019-05-29 | 2020-12-01 | 中国石油天然气股份有限公司 | Well pattern structure for oil reservoir gas injection development and oil extraction method |
CN112127866A (en) * | 2019-06-25 | 2020-12-25 | 中国石油天然气股份有限公司 | Process for developing deep coal bed by using underground coal gasification technology |
CN112127866B (en) * | 2019-06-25 | 2022-08-30 | 中国石油天然气股份有限公司 | Process for developing deep coal bed by using underground coal gasification technology |
CN113803048A (en) * | 2021-08-11 | 2021-12-17 | 太原理工大学 | Coal in-situ separation mining method based on pyrolysis |
CN114186322A (en) * | 2021-12-15 | 2022-03-15 | 安徽理工大学 | Mining earth surface deformation damage blocking control method for thick unconsolidated formation mining area |
CN117307123A (en) * | 2023-11-07 | 2023-12-29 | 中国矿业大学(北京) | Novel underground coal gasification channel and ash removal method |
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EP2843185A1 (en) | 2015-03-04 |
CN102287177A (en) | 2011-12-21 |
EA201400149A1 (en) | 2014-06-30 |
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