CN107676062A - A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate - Google Patents

A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate Download PDF

Info

Publication number
CN107676062A
CN107676062A CN201710988144.6A CN201710988144A CN107676062A CN 107676062 A CN107676062 A CN 107676062A CN 201710988144 A CN201710988144 A CN 201710988144A CN 107676062 A CN107676062 A CN 107676062A
Authority
CN
China
Prior art keywords
well
gas
injection
row
exploitation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
CN201710988144.6A
Other languages
Chinese (zh)
Inventor
袁鹏飞
张晓丽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daqing Dongyou Ruijia Petroleum Technology Co Ltd
Original Assignee
Daqing Dongyou Ruijia Petroleum Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daqing Dongyou Ruijia Petroleum Technology Co Ltd filed Critical Daqing Dongyou Ruijia Petroleum Technology Co Ltd
Priority to CN201710988144.6A priority Critical patent/CN107676062A/en
Publication of CN107676062A publication Critical patent/CN107676062A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/01Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells specially adapted for obtaining from underwater installations
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
    • C09K8/594Compositions used in combination with injected gas, e.g. CO2 orcarbonated gas
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B41/00Equipment or details not covered by groups E21B15/00 - E21B40/00
    • E21B41/0099Equipment or details not covered by groups E21B15/00 - E21B40/00 specially adapted for drilling for or production of natural hydrate or clathrate gas reservoirs; Drilling through or monitoring of formations containing gas hydrates or clathrates
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/164Injecting CO2 or carbonated water
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/30Specific pattern of wells, e.g. optimizing the spacing of wells
    • E21B43/305Specific pattern of wells, e.g. optimizing the spacing of wells comprising at least one inclined or horizontal well
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34Arrangements for separating materials produced by the well
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/70Combining sequestration of CO2 and exploitation of hydrocarbons by injecting CO2 or carbonated water in oil wells

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Mining & Mineral Resources (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Fluid Mechanics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate, belong to the production technique field of gas hydrates.Methods described includes:With reference to geologic information, arrangement row's formula horizontal-well network and supporting completion practice are stored to target, decompression exploitation is implemented until without economic benefit by horizontal well after completion, then ground supply system and downhole injection system are arranged in injection well, segmentation injection carbon dioxide and chemical agent are stored to gas hydrates by injection well, and natural gas and recovered water are collected from producing well;The present invention is applied to low permeability, poor connectivity, the storage that storage is thin, gas hydrates saturation degree is low, horizontal well by storing from arrangement row formula distribution to target, which improves, can employ gas hydrates reserves, injection carbon dioxide is segmented by injection well and chemical agent implements exploitation, gas production efficiency can be improved, improve ultimate recovery, increase economic benefit.

Description

A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate
Technical field
A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate, belong to the production technique of gas hydrates Field.
Background technology
Gas hydrates (natural gas hydrate, abbreviation NGH) are natural gases under certain low temperature, high pressure The non-stoichiometry cage compound formed with water, also referred to as " combustible ice ".1m3Gas hydrates can contain 164m3Methane gas And 0.8m3Water." combustible ice " is the product of growing nonparasitically upon another plant of natural gas, and application is roughly the same with natural gas, is a kind of typical Oil substitutes." combustible ice " easily burns, under equal conditions, energy ratio coal caused by " combustible ice " burning, oil, natural Gas will be higher by decades of times, be described as " belonging to the super energy that end is come ".
The flammable ice reserves very abundant in China, according to investigation, the gas hydrates in China are mainly distributed on south Marine site, Area of The East China Sea, Qinghai-Tibet tundra and northeast tundra.
Artificially break the phase balance condition that gas hydrates are stabilized, promote its decomposition, be that current exploitation is natural The main method of gas hydrate.According to the equilbrium phase diagram of gas hydrates, heating, chemical method, decompression can be generally divided into The class of method three.
Heating:Steam, hot water, hot salt brine or other hot fluid mediums are mainly pumped into natural gas by the method from ground Hydrate reservoir, also using the fire flooding used when exploiting heavy oil or drill string heater can be utilized.Hot production technique it is main not Foot is to cause substantial amounts of heat loss, and efficiency is very low.
Add chemical agent:The chemical agent such as some chemical agents, salt solution, methanol, ethanol, ethylene glycol, glycerine can change Become the phase balance condition of gas hydrate synthesis, reduce hydrate equilibrium temperature.The shortcomings that adding chemical agent maximum is that expense is too expensive. Because the pressure of big midocean gas hydrates is higher, thus the method should not be used.
Voltage drop method:Cause the movement of the stable phase equilibrium line of gas hydrates by reducing pressure, so as to reach Promote the purpose of gas hydrate dissociation.Free gas under exploitation hydrate layer is that the one kind for reducing reservoir pressure has efficacious prescriptions Method, the purpose of control reservoir pressure can be reached additionally by the extraction rate of regulation natural gas, and then controls hydrate The effect of decomposition.The characteristics of voltage drop method maximum is continuous agitation that need not be expensive, thus it is likely to become and opened on a large scale from now on Adopt one of effective ways of gas hydrates.
CN 200910059321.8 disclose it is a kind of by water pump to outside exploitation of gas hydrates well the device of draining and Method, the pressure of gas hydrates layer is reduced by draining, promote the decomposition of gas hydrates layer.It is but simple using drop The decomposition motive force that platen press provides is small, and gas hydrate dissociation causes temperature to reduce, when temperature is reduced to less than 0 DEG C, and also Ice can be caused to block the stagnation with gas hydrate dissociation, while CN 20111048906.4 discloses a kind of drainage and step-down The method exploitation of gas hydrate of heating, the continuous decomposition for promoting hydrate, above two method are all to utilize hydrate point Escaped after solution on gas, water is because deadweight is fallen, and water pump discharges water outside exploitation of gas hydrates well, but actually decomposition gas Substantial amounts of steam is carried during upper ease, upward velocity is very slow, and production efficiency is very low.And level is utilized in CN 20111048906.4 Well combustion heating, combustion heating is dangerous in exploitation of gas hydrates well, has inside and outside exploitation of gas hydrates well flammable Gas, directly heated using naked light abnormally dangerous.
The content of the invention
The present invention relates to a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate, methods described includes:Knot Geologic information is closed, arrangement row's formula horizontal-well network and supporting completion practice are stored to target, implements to be depressured by horizontal well after completion Exploitation then arranges ground supply system and downhole injection system, by injection well to day until without economic benefit in injection well Right gas hydrate storage segmentation injection carbon dioxide and chemical agent, and natural gas and recovered water are collected from producing well;This Invention is applied to that permeability is low, poor connectivity, the storage that storage is thin, gas hydrates saturation degree is low, permeability it is low, connect Property poor, storage is thin, gas hydrates saturation degree is low storage in, due to the restriction of storage condition during injection chemical agent exploitation, It is smaller that chemical agent involves scope, it is difficult to when contacting the gas hydrates in hypotonic duct, and injecting carbon dioxide, due to dioxy It is strong to change the mobility of carbon, involves that scope is larger, the gas hydrates in hypotonic duct can be touched, but due to newly-generated Carbon dioxide hydrate has wrapped gas hydrates and has prevented the displacement of next step, carbon dioxide replacement reaction speed compared with Slowly;It is that therefore the present invention combines two kinds of recovery methods, the connectedness for involving duct by injecting carbon dioxide increase to be difficult to originally, Catalytic decomposition is implemented to the gas hydrates in duct by injecting chemical agent, can improve can employ gas hydrates storage Amount, gas production efficiency can be improved, improve ultimate recovery, increase economic benefit.
To achieve these goals, the invention provides the side that a kind of row's formula horizontal well mixed phase drives exploitation of gas hydrate Method, methods described comprise the steps:
Step 1, arrangement row's formula horizontal-well network, with reference to geologic information, arrangement row's formula horizontal-well network, horizontal well are stored to target It is divided into injection well and producing well, gas hydrates reserves can be employed to improve by arranging formula level distribution well;
Step 2, completion practice, row's formula horizontal-well network arrangement carry out supporting completion practice after completing;
Step 3, decompression exploitation, after supporting completion practice, the supporting ground system of located production wells, to injection well and producing well Implement decompression exploitation, until without economic benefit;
Step 4, arrangement injected system, injected system include ground supply system and downhole injection system;
Step 5, displacement exploitation, segmentation injection carbon dioxide and chemical agent are stored to gas hydrates by injection well, And collect natural gas and stratum water from producing well.
Formula horizontal-well network is arranged in the step 1 to be included:Injection well direction described in row's formula horizontal-well network and the life It can be in the same direction or reverse to produce well direction;The horizontal segment of injection well and producing well in row's formula horizontal-well network Can be isometric or non-isometric;Injection well and producing well can be aligned fashions in row's formula horizontal-well network Or be dislocatedly distributed;The injection well horizontal segment depth and the producing well horizontal segment depth can be it is contour, The injection well horizontal segment can also be located above or below the producing well horizontal segment;The distance between each well is according to storage bar Part can change within the specific limits.
Preferably, row's formula horizontal-well network arrangement scope is:Horizontal-well network spacing range 300-1000 rice, horizontal segment length Spend scope 500-2000 rice.
Supporting completion practice is divided into straight well section completion and horizontal segment completion in the step 2, straight in the straight well section completion Well section depth is more than horizontal segment depth 5-30 rice, forms liquid storage chamber, to realize that air water point is adopted, reduces produced gas water content, and press down Gas hydrates are formed in sleeve pipe processed;The horizontal segment completion is well-case perforating completion, perforation fragment position, perforating depth, is penetrated Hole density can be adjusted according to actual storage situation;Tripping in electricity is latent in the injection well and producing well straight well section during operation Pump, tripping in is to straight well section bottom liquid storage chamber, and tripping in sand control installation, sand control installation can prevent gas hydrate dissociation from producing Sandstone enter straight well section in, prevent sandstone damage underground equipment;Specific implementation process is the tripping in sand control into horizontal well successively Device, centralizer, electric submersible pump and power cable, the sand control installation, centralizer, electric submersible pump and power cable are conventional Downhole tool, model can be adapted to according to actual storage situation selection.
The supporting ground system of producing well includes electric power system, produced water treatment system, produced gas processing system in the step 3 System and control system.
The electric power system includes power supply, frequency converter, is sequentially connected, passed through by power cable and production wellhead oil pipe entrance Power converter output is adjusted, and then adjusts electric submersible pump in shaft bottom drain age velocity;The power supply include generator, commercial power and Various normal power supplies.
The produced water treatment system includes water storage device, water treatment facilities, control valve, temperature sensor, pressure and passed Sensor, fluid flowmeter, it is sequentially connected via liquid line and the outlet of production wellhead oil pipe, is passed by fluid flowmeter, pressure Sensor and temperature sensor real-time collecting electric submersible pump discharge opeing data, displacement is implemented to control by control valve, at water Reason device is filtered to recovered water, degassing process, the water after filtering is fed into water storage device to treat to handle in next step, the storage Metering device is provided with inside water installations, to monitor water-holding quantity inside water storage device;The water storage device include water pot and its He has the container for depositing water storage function, and the metering device, which includes tank gage and other, has the device for measuring water level function, The water treatment facilities is included with the conventional water treatment equipment that airway dysfunction is dissolved in filtering, decomposition water, the control valve, temperature It is conventional equipment to spend sensor, pressure sensor, fluid flowmeter, liquid line.
The extraction gas processing system includes warehousing and transportation facilities, gas treatment equipment, gas-liquid separator, control valve, temperature Sensor, pressure sensor, gas flowmeter are spent, production wellhead cannula exit is connected to via gas transmission line successively, passes through gas Flowmeter body, pressure sensor and temperature sensor real-time collecting sleeve pipe gas production data, gas production is implemented by control valve Control, gas-liquid separation processing is carried out to produced gas by gas-liquid separator, the natural gas after separation feeds natural gas treatment plant Next step processing, including filtration treatment, desulfurization process, dewater treatment are carried out, the natural gas after processing feeds warehousing and transportation facilities and carried out Transport;The warehousing and transportation facilities include gas transmission line, pressure vessel and other there is the conventional equipment of natural gas accumulating function, it is described Gas treatment equipment includes The conventional equipment with gas-liquid separating function, the control valve, temperature sensor, pressure sensor, gas flowmeter, gas transmission Pipeline is conventional equipment.
It is connected between the water treatment facilities and gas-liquid separator by gas transmission line with liquid line, the appendix Line is provided with gas flowmeter, and the liquid line is provided with fluid flowmeter, caused natural after being deaerated in water treatment facilities Gas feeds gas-liquid separator, and the water that gas-liquid separator separates go out feeds water treatment facilities and is further processed.
The control system includes controller and signal receiver, passes through frequency converter in signal-transmitting cable and electric power system It is connected, to monitoring frequency converter working condition in real time, and remote control is implemented to frequency converter by controller, passed by signal Transmission cable connects with control valve, temperature sensor, pressure sensor, fluid flowmeter, metering device in produced water treatment system Connect, monitoring produced water treatment working state of system is implemented by controller, and realize and produced water treatment system remote is controlled, lead to Signal-transmitting cable is crossed with control valve, temperature sensor, pressure sensor, gas flowmeter in extraction gas processing system to connect Connect, monitoring extraction gas processing system working condition is implemented by controller, and realize to producing gas processing system remote control;Institute State controller include computer, tablet personal computer and other there is the conventional equipment of control function, the signal receiver is tool There is signal to receive, the conventional equipment of transformation function.
The decompression exploitation is embodied as, and shaft bottom is drawn water by electric submersible pump in injection well and producing well, passes through oil pipe With the gas production of casing annulus part, underground electric submersible pump discharge capacity is implemented to adjust by frequency converter, when gas production is too low or other After reason causes no economic benefit, injection well Ground device is removed one by one, and arrange injected system.
Ground supply system described in the step 4 includes chemical agent system, carbon dioxide system and control system.
The chemical agent system includes water treatment facilities, agitating device, chemical agent storage tank, control valve, water storage device, meter Measure device, supercharging device, fluid flowmeter, temperature sensor, pressure sensor, the water treatment facilities by liquid line with Agitating device is connected, and the chemical agent storage tank is connected by liquid line with agitating device, and the liquid line is provided with Control valve and fluid flowmeter, the agitating device, water storage device, supercharging device, fluid flowmeter, temperature sensor, pressure Force snesor is sequentially connected via liquid line and injection well head;The water treatment facilities connects water source, and injection water was carried out Filter, the processing of sudden and violent oxygen, the water after filtering is fed into agitating device, metering device is provided with inside the water storage device, to monitor storage Water-holding quantity inside water installations, the supercharging device provide operating pressure, the control valve, fluid flow for injection chemical agent Meter, pressure sensor and temperature sensor record chemical agent systems operations data in real time;The water source include well water, seawater, Layer recovered water and other conventional source waters, the water treatment facilities are included with filtering, the conventional water treatment equipment of sudden and violent oxygen function, institute Stating chemical agent storage tank includes the conventional vessel with chemical agent store function, and the water storage device, which includes water pot and other, to be had The container of water storage function is deposited, the metering device, which includes tank gage and other, has the device for measuring water level function, the increasing Pressure device include water pump, pump truck and other there is the conventional supercharging device of liquid function of increasing pressure, the control valve, TEMP Device, pressure sensor, fluid flowmeter, liquid line are conventional equipment.
The carbon dioxide system includes carboloy dioxide storage plant, supercharging device, control valve, gas flowmeter, temperature Sensor, pressure sensor are spent, the carboloy dioxide storage plant is connected by gas line with supercharging device entrance, described Supercharging device outlet by gas line with inject well head is connected, the control valve, gas flowmeter, temperature sensor, Positioned at connection supercharging device with injecting on the gas line of well head, the supercharging device carries pressure sensor for injection carbon dioxide For operating pressure, the control valve, gas flowmeter, pressure sensor and temperature sensor record carbon dioxide system in real time Operational data;The carboloy dioxide storage plant, which includes gas cylinder and other, has the storage carbon functional conventional equipment of titanium dioxide, institute Stating supercharging device and including air pump and other has the conventional supercharging device of gas boosting function, the control valve, TEMP Device, pressure sensor, gas flowmeter, gas line are conventional equipment.
The control system includes controller and signal receiver, by signal-transmitting cable with being adjusted in chemical agent system Valve, temperature sensor, pressure sensor, fluid flowmeter, supercharging device, metering device connection, implement to supervise by controller Chemical agent working state of system is surveyed, and realizes and chemical agent system remote is controlled;Pass through signal-transmitting cable and carbon dioxide system Supercharging device, control valve, temperature sensor, pressure sensor, gas flowmeter connection in system, implement to monitor by controller Carbon dioxide system working condition, and realize to carbon dioxide system remote control;The controller includes computer, flat board electricity Brain and other there is the conventional equipment of control function, the signal receiver be received with signal, the routine of transformation function Equipment.
Downhole injection system in the step 4, including insulated tubing, centralizer, packer and horn mouth, in injection well Interior, tripping in horn mouth, insulated tubing, packer, centralizer, horn mouth seal packer after reaching predeterminated position successively, with Form closed Injection Space, the packer, centralizer can be one or multiple, and the packer, centralizer are Can be conventional equipment with the matching used conventional equipment of insulated tubing, the insulated tubing, horn mouth, according to the specific feelings of storage Condition can adjust different model.
Displacement exploitation specific implementation process is that the displacement stages of mining is to be stored up to gas hydrates in the step 5 0.3 times of pore volume gaseous carbon dioxide is injected in Tibetan, 0.1 times of pore volume chemical agent is subsequently injected into, then implements titanium dioxide Carbon and chemical agent are alternately injected with foregoing injection rate, and collect natural gas and stratum water from producing well;The carbon dioxide is gas State carbon dioxide;The source water is handled through sudden and violent oxygen can reduce content of oxygen dissolved in water, and improve water source coolant-temperature gage, injection storage After can increase gas hydrate dissociation speed;The chemical agent composition is for 5% mass than methanol, 5% mass than ethanol, 3% For quality than DTAC, remaining components are that source water, methanol and ethanol can change hydration as catalyst The phase balance condition that thing is formed, hydrate equilibrium temperature is reduced, to increase decomposition of hydrate speed, trimethyl chlorination Ammonium uses as clay stabilizer, can prevent clay particle expansion pollution to caused by storage in storage.
In horizontal production well gas production process, by controlling injection well injection rate and producing well to produce gas and water discharge capacity, and then adjust Whole producing well hydrodynamic face and flowing bottomhole pressure (FBHP), between making producing well flowing bottomhole pressure (FBHP) holding 1.5-4Mpa, pass through and adjust rational row Speed is adopted, control produced gas water content, temperature, to suppress to be formed gas hydrates in pit shaft, and keeps higher gas production speed Degree;Carbon dioxide content in periodic monitor produced gas, reduction aerogenesis can be taken when carbon dioxide content is too high in production process Speed, reduce carbon dioxide injection amount, increase chemical agent injection rate and other regulating measures.
Beneficial effect of the present invention is:
1) present invention is exploited by voltage drop method to injection well and producing well first, is exploited with ensuring to drive in follow-up mixed phase Shi Buhui because hydrate largely decomposes and occur bottom pressure is too high, the too fast danger to caused by underground equipment of natural gas flow velocity Evil, improve the security of exploitation of gas hydrates.
2) present invention production bottom be provided with liquid storage chamber, the water generated in recovery process can into liquid storage chamber and via Electric submersible pump is discharged, and is made output gas avoid mixing with water in underground, can effectively be reduced the water content of natural gas in oil jacket annular space, is increased Gas upward velocity, and then improve production efficiency.
3) present invention stores segmentation injection carbon dioxide and chemical agent to gas hydrates by downhole injection system, can Suitable for permeability is low, poor connectivity, the storage that storage is thin, gas hydrates saturation degree is low, increased by injecting carbon dioxide Add the connectedness for being difficult to involve duct originally, catalytic decomposition implemented to the gas hydrates in duct by injecting chemical agent, Can improve can employ gas hydrates reserves, can improve gas production efficiency, improve ultimate recovery, increase economic benefit, can add Fast gas hydrate dissociation speed simultaneously suppresses clay swelling and polluted to caused by storage, and being segmented the mode of injection can save into This, and the inventive method job safety is reliable.
4) present invention can adopt gas hydrates reserves by storing the horizontal-well network raising of arrangement row's formula to target, relative to Traditional straight well well pattern, horizontal well patterns, row's formula horizontal-well network of the present invention can improve in storage to a greater extent can adopt gas water Compound reserves.
Brief description of the drawings
In order to illustrate more clearly of technical scheme, the required accompanying drawing used in description will be made below simple Ground introduction, it should be apparent that, drawings in the following description are only some embodiments of the present invention, for those skilled in the art For, it can also obtain other accompanying drawings according to these accompanying drawings on the premise of not paying creative work.
Fig. 1 is horizontal-well network aligned fashion schematic diagram in the same direction.
Fig. 2 is the reverse aligned fashion schematic diagram of horizontal-well network.
Fig. 3 is that horizontal-well network is dislocatedly distributed schematic diagram in the same direction.
Fig. 4 is that horizontal-well network is reversely dislocatedly distributed schematic diagram.
Fig. 5 is horizontal segment depth schematic diagram.
Fig. 6 is decompression exploitation completion schematic diagram.
Fig. 7 is producing well ground configuration schematic diagram.
Fig. 8 is injection well ground supply system schematic.
Fig. 9 is downhole injection system schematic diagram.
Drawing reference numeral:1st, injection well 2, producing well 3, gas hydrates reservoir 4, overlying rock 5, lower rock stratum 6, straight well Section 7, horizontal segment 8, sleeve pipe 9, oil pipe 10, perforated interval 11, sand control installation 12, electric submersible pump 13, centralizer 14, liquid storage chamber 15, power supply 16th, power cable 17, frequency converter 18, production wellhead 19, fluid flowmeter 20, pressure sensor 21, temperature sensor 22, liquid Pipeline 23, control valve 24, water treatment facilities 25, water storage device 26, metering device 27, gas transmission line 28, gas flowmeter 29, Gas-liquid separator 30, gas treatment equipment 31, warehousing and transportation facilities 32, controller 33, signal receiving device 34, signal-transmitting cable 35th, agitating device 36, methanol tank 37, ethanol storage tank 38, supercharging device 39, injection well head 40, carboloy dioxide storage plant 41, Insulated tubing 42, packer 43, horn mouth.
Embodiment
The embodiment of the present invention provides a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate, methods described bag Include:With reference to geologic information, arrangement row's formula horizontal-well network and supporting completion practice are stored to target, is implemented after completion by horizontal well Decompression exploitation then arranges ground supply system and downhole injection system in injection well, passes through injection well until without economic benefit Gas hydrates are stored with segmentation injection carbon dioxide and chemical agent, and natural gas and recovered water are received from producing well Collection.
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.Based on this Embodiment in invention, the every other reality that those of ordinary skill in the art are obtained under the premise of creative work is not made Example is applied, belongs to the scope of protection of the invention.
The embodiments of the invention provide a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate, methods described Comprise the following steps:
Step 1, arrangement row's formula horizontal-well network, with reference to geologic information, arrangement row's formula horizontal-well network, horizontal well are stored to target It is divided into injection well and producing well, gas hydrates reserves can be employed to improve by arranging formula level distribution well, arranges formula horizontal well Net has following several arrangement modes:
As shown in figure 1, Fig. 1 is horizontal-well network aligned fashion schematic diagram in the same direction, injection well 1 is distributed in the same direction with producing well 2, note It is in laterally aligned distribution to enter the horizontal segment of well 1 with the horizontal segment of producing well 2.
As shown in Fig. 2 Fig. 2 is the reverse aligned fashion schematic diagram of horizontal-well network, injection well 1 is reversely distributed with producing well 2, note It is in laterally aligned distribution to enter the horizontal segment of well 1 with the horizontal segment of producing well 2.
It is dislocatedly distributed in the same direction schematic diagram as shown in figure 3, Fig. 3 is horizontal-well network, injection well 1 is distributed in the same direction with producing well 2, note Enter the horizontal segment of well 1 and the horizontal segment of producing well 2 to be distributed in transversion malposition, and after being located at the heel of injection well 1 at the heel of producing well 2 Side.
Reversely it is dislocatedly distributed schematic diagram as shown in figure 4, Fig. 4 is horizontal-well network, injection well 1 is reversely distributed with producing well 2, note Enter the horizontal segment of well 1 and the horizontal segment of producing well 2 to be distributed in transversion malposition, and before being located at the heel of injection well 1 at the tiptoe of producing well 2 Side.
Injection well horizontal segment is placed with following several ways with producing well horizontal segment depth, as shown in figure 5, deep for horizontal segment Spend schematic diagram:
Fig. 5 A are that the horizontal segment depth of setting of injection well 1 is less than the horizontal segment depth of setting of producing well 2, injection well 1 and producing well 2 Horizontal segment is in gas hydrates reservoir 3, under overlying rock 4, on lower rock stratum 5.
Fig. 5 B are that the horizontal segment depth of setting of injection well 1 is equal to the horizontal segment depth of setting of producing well 2, injection well 1 and producing well 2 Horizontal segment is in gas hydrates reservoir 3, under overlying rock 4, on lower rock stratum 5.
Fig. 5 C are that the horizontal segment depth of setting of injection well 1 is more than the horizontal segment depth of setting of producing well 2, injection well 1 and producing well 2 Horizontal segment is in gas hydrates reservoir 3, under overlying rock 4, on lower rock stratum 5.
Step 2, completion practice, row's formula horizontal-well network arrangement carry out supporting completion practice after completing, and decompression as shown in Figure 6 is opened Completion schematic diagram is adopted, the straight well section 6 pierces depth and pierces depth more than horizontal segment 7, forms liquid storage chamber 14;The horizontal segment 7 Completion is well-case perforating completion, and perforated interval 10 is located on horizontal segment 7;Tripping in electricity is latent in injection well 1 and the straight well section 6 of producing well 2 Pump 12, tripping in the bottom liquid storage chamber 14 of straight well section 6, and tripping in sand control installation 11, are drawn water to shaft bottom by oil pipe 9, pass through oil pipe 9 With the annular section gas production of sleeve pipe 8;Specific implementation process is tripping in sand control installation 11, centralizer 13, electricity are latent into horizontal well successively Pump 12 and power cable, do not regard in power cable figure.
Step 3, decompression exploitation, after supporting completion practice, the supporting ground system of located production wells, to injection well and producing well Implement decompression exploitation, until without economic benefit, producing well ground configuration schematic diagram as shown in Figure 7, the supporting ground of producing well System includes electric power system, produced water treatment system, extraction gas processing system and control system.
The electric power system includes power supply 15, frequency converter 17, by power cable 16 and the entrance of 18 oil pipe of production wellhead 9 successively Connection, by adjusting the power output of frequency converter 17, and then electric submersible pump 12 is adjusted in shaft bottom drain age velocity.
The produced water treatment system includes water storage device 25, water treatment facilities 24, control valve 23, temperature sensor 21st, pressure sensor 20, fluid flowmeter 19, it is connected by liquid line 22 with the outlet of the oil pipe 9 of production wellhead 18, passes through liquid Flowmeter body 19, pressure sensor 20 and the discharge opeing data of 21 real-time collecting electric submersible pump of temperature sensor 12, pass through control valve 23 Displacement is implemented to control, recovered water filtered by water treatment facilities 24, degassing process, the water after filtering is fed into storage Water installations 25 are to treat to handle in next step, and the inside of water storage device 25 is provided with metering device 26, to monitor in water storage device 25 Portion's water-holding quantity.
The extraction gas processing system includes warehousing and transportation facilities 31, gas treatment equipment 30, gas-liquid separator 29, regulating valve Door 23, temperature sensor 21, pressure sensor 20, gas flowmeter 28, are connected to production wellhead via gas transmission line 27 successively 18 sleeve pipes 8 export, by gas flowmeter 28, pressure sensor 20 and the gas production data of 21 real-time collecting sleeve pipe of temperature sensor 8, Gas production is implemented to control by control valve 23, gas-liquid separation processing, separation are carried out to produced gas by gas-liquid separator 29 Natural gas afterwards feeds natural gas treatment plant 30 and carries out next step processing, including filtration treatment, desulfurization process, dewater treatment, Natural gas after processing feeds warehousing and transportation facilities 31 and transported, the gas-liquid separator 29, gas treatment equipment 30 and accumulating Equipment 31 is connected by gas transmission line 27, and gas flowmeter 28 is provided with pipeline.
It is connected between the water treatment facilities 24 and gas-liquid separator 29 by gas transmission line 27 with liquid line 22, institute State gas transmission line 27 and be provided with gas flowmeter 28, the liquid line 22 is provided with fluid flowmeter 19, water treatment facilities 24 Caused natural gas feeds gas-liquid separator 29 after middle degassing, and the water that gas-liquid separator 29 is isolated feeds water treatment facilities 24 and entered Row is handled in next step.
The control system includes controller 32 and signal receiver 33, by signal-transmitting cable 34 and electric power system Frequency converter 17 is connected, to the monitoring working condition of frequency converter 17, and being implemented remotely to frequency converter 17 by controller 32 in real time Control, pass through control valve 23, temperature sensor 21, pressure sensor in signal-transmitting cable 34 and produced water treatment system 20th, fluid flowmeter 19, metering device 26 connect, and implement monitoring produced water treatment working state of system by controller 32, and Realize to produced water treatment system remote control, by signal-transmitting cable 34 with extraction gas processing system in control valve 23, Temperature sensor 21, pressure sensor 20, gas flowmeter 28 connect, and implement monitoring extraction gas processing system by controller 32 Working condition, and realize to producing gas processing system remote control.
Step 4, arrangement injected system, injected system include ground supply system and downhole injection system;After decompression exploitation, Injection well Ground device is removed one by one, and arranges ground supply system, injection well ground supply system signal as shown in Figure 8 Figure, the ground supply system include chemical agent system, carbon dioxide system and control system.
The chemical agent system includes water treatment facilities 24, agitating device 35, methanol tank 36, ethanol storage tank 37, regulation Valve 23, water storage device 25, metering device 26, supercharging device 38, fluid flowmeter 19, temperature sensor 21, pressure sensor 20, the water treatment facilities 24 is connected by liquid line 22 with agitating device 35, the methanol tank 36, ethanol storage tank 37 It is connected by liquid line 22 with agitating device 35, the liquid line 22 is provided with control valve 23 and fluid flowmeter 19, the agitating device 35, water storage device 25, supercharging device 38, fluid flowmeter 19, temperature sensor 21, pressure sensor 20 are sequentially connected via liquid line 22 and injection well head 39;The water treatment facilities 24 connects water source, and injection water was carried out Filter, the processing of sudden and violent oxygen, the water after filtering being fed into agitating device 35, the inside of water storage device 25 is provided with metering device 26, to The inside water-holding quantity of water storage device 25 is monitored, the supercharging device 38 provides operating pressure, the control valve 23, liquid for injection water Flowmeter body 19, pressure sensor 20 and temperature sensor 21 record chemical agent systems operations data in real time.
The carbon dioxide system includes carboloy dioxide storage plant 40, supercharging device 38, control valve 23, gas flow Meter 28, temperature sensor 21, pressure sensor 20, the carboloy dioxide storage plant 40 pass through gas line 27 and supercharging device 38 entrances are connected, and the outlet of supercharging device 38 is connected by gas line 27 with injection well head 39, the control valve 23rd, gas flowmeter 28, temperature sensor 21, pressure sensor 20 are positioned at connection supercharging device 38 and the gas for injecting well head 39 On pipeline 27, the supercharging device 38 provides operating pressure, the control valve 23, gas flowmeter for injection carbon dioxide 28th, pressure sensor 20 and temperature sensor 21 record carbon dioxide system operational data in real time.
The control system includes controller 32 and signal receiver 33, passes through signal-transmitting cable 34 and chemical agent system Middle control valve 23, temperature sensor 21, pressure sensor 20, fluid flowmeter 19, supercharging device 38, metering device 26 connect Connect, monitoring chemical agent working state of system is implemented by controller 32, and realize and chemical agent system remote is controlled;Pass through signal Transmission cable 34 and supercharging device 38, control valve 23, temperature sensor 21, pressure sensor 20, gas in carbon dioxide system Flowmeter body 28 connects, and implements monitoring carbon dioxide system working condition by controller 32, and realize to carbon dioxide system Remote control.
Downhole injection system in the step 4, including insulated tubing 41, centralizer 13, packer 42 and horn mouth 43, such as Shown in Fig. 9, downhole injection system schematic diagram, injecting into well, successively tripping in horn mouth 43, insulated tubing 41, packer 42, help Positive device 13, horn mouth 43 seals packer 42 after reaching predeterminated position, to form closed Injection Space.
Step 5, displacement exploitation, injection carbon dioxide and chemistry are segmented to gas hydrates reservoir 3 by injection well 1 Agent, the displacement stages of mining are that 0.3 times of pore volume gaseous carbon dioxide is injected in being stored to gas hydrates, then note Enter 0.1 times of pore volume chemical agent, then implement carbon dioxide and chemical agent and alternately injected with foregoing injection rate;Inject titanium dioxide Carboloy dioxide storage plant 40 is exported into opening during carbon, supercharging device 38 is fed carbon dioxide into by gas line 27, passed through Supercharging device 38 provides operating pressure for injection carbon dioxide, is injected via injection well head 39 in gas hydrates reservoir 3;Note Implement filtering, the processing of sudden and violent oxygen when entering chemical agent to source water by water treatment facilities 24, the water after processing is fed into agitating device 35, and control valve 23 is opened, the methanol in methanol tank 36 flows into agitating device via control valve 23, fluid flowmeter 19 In 35, the ethanol in ethanol storage tank 37 is flowed into agitating device 35 via control valve 23, fluid flowmeter 19, and is filled from stirring Put 35 entrances and add DTAC, the source water, methanol, ethanol, DTAC exist It is sufficiently stirred in agitating device 35, and gas hydrates storage is injected via water storage device 25, supercharging device 38, injection well head 39 In layer 3, and natural gas and stratum water are collected from producing well 2;The chemical agent composition is that 5% mass compares second than methanol, 5% mass Than DTAC, remaining components are source water for alcohol, 3% mass.

Claims (8)

1. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate, it is characterised in that methods described includes following Step:
Step 1, arrangement row's formula horizontal-well network, with reference to geologic information, arrangement row's formula horizontal-well network is stored to target, horizontal well is divided into Injection well and producing well, gas hydrates reserves can be employed to improve by arranging formula level distribution well;
Step 2, completion practice, row's formula horizontal-well network arrangement carry out supporting completion practice after completing;
Step 3, decompression exploitation, after supporting completion practice, the supporting ground system of located production wells, implement to injection well and producing well Decompression exploitation, until without economic benefit;
Step 4, arrangement injected system, injected system include ground supply system and downhole injection system;
Gas hydrates are stored and are segmented injection carbon dioxide and chemical agent by step 5, displacement exploitation by injection well, and from Producing well collects natural gas and stratum water.
2. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate as claimed in claim 1, it is characterised in that institute It can be in the same direction or reverse that injection well horizontal segment bearing of trend, which is stated, with the producing well horizontal segment bearing of trend; The injection well horizontal segment depth and the producing well horizontal segment depth can be contour, and the injection well horizontal segment can also Above or below the producing well horizontal segment.
3. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate as claimed in claim 1, it is characterised in that institute State supporting completion practice and be divided into straight well section completion and horizontal segment completion, straight well section depth is more than level in the straight well section completion Section, form liquid storage chamber;The horizontal segment completion is well-case perforating completion.
4. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate as claimed in claim 1, it is characterised in that institute It is the tripping in electric submersible pump in injection well and producing well to state decompression exploitation, and shaft bottom is drawn water by oil pipe, passes through oil pipe and sleeve ring Empty part gas production.
5. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate as claimed in claim 1, it is characterised in that institute Stating the supporting ground system of producing well in decompression exploitation includes electric power system, produced water treatment system, extraction gas processing system and control System processed, the electric power system include power supply, frequency converter;The produced water treatment system include water storage device, water treatment facilities, Control valve, temperature sensor, pressure sensor, fluid flowmeter;The extraction gas processing system includes warehousing and transportation facilities, natural Gas disposal equipment, gas-liquid separator, control valve, temperature sensor, pressure sensor, gas flowmeter;The control system Including controller and signal receiver.
6. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate as claimed in claim 1, it is characterised in that institute Stating ground supply system includes chemical agent system, carbon dioxide system and control system, and the chemical agent system includes water process Device, agitating device, chemical agent storage tank, control valve, water storage device, metering device, supercharging device, fluid flowmeter, temperature Sensor, pressure sensor;The carbon dioxide system includes carboloy dioxide storage plant, supercharging device, control valve, gas Flowmeter, temperature sensor, pressure sensor;The control system includes controller and signal receiver.
7. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate as claimed in claim 1, it is characterised in that institute Stating downhole injection system includes insulated tubing, centralizer, packer and horn mouth.
8. a kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate as claimed in claim 1, it is characterised in that institute It is to inject 0.3 times of pore volume gaseous carbon dioxide in being stored to gas hydrates to state displacement stages of mining, is subsequently injected into 0.1 Times pore volume chemical agent, then implement carbon dioxide and chemical agent and alternately injected with foregoing injection rate, and collected from producing well Natural gas and stratum water;The carbon dioxide is gaseous carbon dioxide;The chemical agent composition is 5% mass than methanol, 5% matter For amount than ethanol, 3% mass than DTAC, remaining components are source water.
CN201710988144.6A 2017-10-23 2017-10-23 A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate Withdrawn CN107676062A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710988144.6A CN107676062A (en) 2017-10-23 2017-10-23 A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710988144.6A CN107676062A (en) 2017-10-23 2017-10-23 A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate

Publications (1)

Publication Number Publication Date
CN107676062A true CN107676062A (en) 2018-02-09

Family

ID=61141329

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710988144.6A Withdrawn CN107676062A (en) 2017-10-23 2017-10-23 A kind of method that row's formula horizontal well mixed phase drives exploitation of gas hydrate

Country Status (1)

Country Link
CN (1) CN107676062A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1944949A (en) * 2006-08-09 2007-04-11 中国石油大学(华东) Method for recovering sea bottom hydrate by single well heat injection circulation
CN101666286A (en) * 2009-09-28 2010-03-10 中国海洋石油总公司 System for integrally exploiting marine energy resource
CN103603638A (en) * 2013-11-13 2014-02-26 大连理工大学 Natural gas hydrate CO2 substitution extraction method combined with depressurization
CN105545273A (en) * 2016-01-23 2016-05-04 吉林大学 Device and method for exploiting terrestrial natural gas hydrates through CO2 fracturing and displacing
CN105625998A (en) * 2016-02-02 2016-06-01 西南石油大学 Reverse production method and production equipment for seafloor natural gas hydrate stable layer
CN106677745A (en) * 2016-12-02 2017-05-17 中国石油大学(华东) Process method combining natural gas hydrate depressurizing development with CO2 storage

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1944949A (en) * 2006-08-09 2007-04-11 中国石油大学(华东) Method for recovering sea bottom hydrate by single well heat injection circulation
CN101666286A (en) * 2009-09-28 2010-03-10 中国海洋石油总公司 System for integrally exploiting marine energy resource
CN103603638A (en) * 2013-11-13 2014-02-26 大连理工大学 Natural gas hydrate CO2 substitution extraction method combined with depressurization
CN105545273A (en) * 2016-01-23 2016-05-04 吉林大学 Device and method for exploiting terrestrial natural gas hydrates through CO2 fracturing and displacing
CN105625998A (en) * 2016-02-02 2016-06-01 西南石油大学 Reverse production method and production equipment for seafloor natural gas hydrate stable layer
CN106677745A (en) * 2016-12-02 2017-05-17 中国石油大学(华东) Process method combining natural gas hydrate depressurizing development with CO2 storage

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
吴传芝等: "天然气水合物开采技术研究进展", 《地质科技情报》 *
杜冰鑫等: "天然气水合物勘探与开发进展", 《天然气勘探与开发》 *

Similar Documents

Publication Publication Date Title
CN107575195A (en) A kind of method that gas hydrates parallel water horizontal well mixed phase drives exploitation
CN107514248A (en) A kind of method of gas hydrates parallel water horizontal well chemical flooding exploitation
CN105003237B (en) Geothermal exploitation of natural gas hydrates and CO2Integrated device and method for exhaust gas reinjection treatment
CN107542440A (en) A kind of method of U-shaped well microwave heating exploitation of gas hydrate
CN107676061A (en) A kind of method of parallel water horizontal well exploitation offshore natural gas hydrate
CN107542441A (en) A kind of method of parallel water horizontal well hot-water flooding exploitation of gas hydrate
CN107514245A (en) A kind of method of gas hydrates row formula horizontal wells
CN103410488B (en) Gas hydrates water pumping gas production quarrying apparatus and exploitation method thereof
CN107676060A (en) A kind of method of the U-shaped well microwave heating exploitation of gas hydrates
CN101089362B (en) Improved steam oil production method
CN107795302B (en) A kind of Gas Hydrate In Sea Areas decompression quarrying apparatus and its recovery method
RU2060378C1 (en) Method for developing oil stratum
CN107575193A (en) A kind of method of offshore natural gas hydrate row formula horizontal wells
CN107701150A (en) A kind of method of offshore natural gas hydrate parallel water horizontal well exploitation
CN107575201A (en) A kind of method of gas hydrates parallel water horizontal well microwave heating exploitation
CN109695441A (en) A kind of method of parallel water horizontal well microwave heating exploitation of gas hydrate
CN107575196A (en) A kind of method that gas hydrates row's formula horizontal well mixed phase drives exploitation
CN105971573A (en) System and method for automatically generating CO2 foam and exploiting coalbed methane in huff-puff mode underground
CN107575200A (en) A kind of method of gas hydrates parallel water horizontal well exploitation
CN107558977A (en) A kind of method of row's formula horizontal well microwave heating exploitation of gas hydrate
CN107740686A (en) A kind of method that parallel water horizontal well mixed phase drives exploitation of gas hydrate
CN107503723A (en) A kind of method of gas hydrates row's formula horizontal well chemical flooding exploitation
CN112081559A (en) Device and method for extracting natural gas hydrate by depressurization and double-pipe injection of modified fluid
CN112983408B (en) Device and method for purging inert gas for preventing and controlling solid phase deposition during depressurization exploitation of hydrate
CN104912527A (en) Construction process for gas producing system in oil well layer

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication

Application publication date: 20180209

WW01 Invention patent application withdrawn after publication