CN202220587U - Three-dimensional multiple-well combined exploitation experiment device for natural gas hydrate - Google Patents
Three-dimensional multiple-well combined exploitation experiment device for natural gas hydrate Download PDFInfo
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- CN202220587U CN202220587U CN2011203316224U CN201120331622U CN202220587U CN 202220587 U CN202220587 U CN 202220587U CN 2011203316224 U CN2011203316224 U CN 2011203316224U CN 201120331622 U CN201120331622 U CN 201120331622U CN 202220587 U CN202220587 U CN 202220587U
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Abstract
The utility model discloses a three-dimensional multiple-well combined exploitation experiment device for natural gas hydrate, which comprises the following components: a three-dimensional high-pressure reaction vessel, an inlet control unit, an outlet control unit and a data processing unit. The three-dimensional high-pressure reaction vessel is provided with a plurality of wells which extends into the inner part of a simulation chamber. The three-dimensional high-pressure reaction vessel comprises a central vertical well and a plurality of vertical side wells. The simulation chamber is divided into n horizontal surfaces in a vertical direction. Vertical well pipes extend into the horizontal surfaces with different thicknesses in the simulation chamber respectively. Multiple-well combined exploitation for the hydrate can be simulated. Various exploitation principles and exploitation trends can be researched integrally, and furthermore various exploitation methods are optimized and evaluated comprehensively. The experiment device realizes multiple-well exploitation simulation for hydrate through experiment, thereby expanding the three-dimensional simulation experiment, and providing experiment base and basis for large-scale natural gas hydrate exploitation.
Description
Technical field
The utility model relates to the exploitation of gas hydrates field, the three-dimensional many wells unitized production of in particular a kind of gas hydrates experimental facilities.
Background technology
Gas hydrates are meant a kind of cage shape crystalline solid that natural gas and water generate under uniform temperature and pressure, it meets fire is incendivity, is commonly called as " combustible ice ".Along with people's deepens continuously to hydrate research, and the influence that the characteristic of hydrate reaches environment is the human knowledge more and more, the more important thing is that its value as a kind of effective alternative energy source is also beneficial apparent outstanding.
Gas hydrates can be present in occurring in nature in many ways, and based on the characteristics of gas hydrates, it is different with the exploitation of the conventional traditional energy.Show that it is solid that hydrate buries on the ocean bottom, molecular configuration changes in recovery process, becomes gas from solid.That is to say that hydrate undergoes phase transition in recovery process.At present the developing thought of the relevant gas hydrates of great majority all are to consider that at first the gas hydrates how will contain in deposit decompose basically, and then with natural gas extraction to ground.In general, breaking the temperature, pressure condition of gas hydrates stable existence artificially, cause it to decompose, is the main method of methane resource amount in the present development of natural gas hydrate.Existing exploitation method can be divided into following three kinds substantially:
First kind, heating exploitation method; With method mainly is that steam, hot water, hot salt brine or other hot fluid are pumped into the gas hydrates reservoir from ground, or adopts many methods such as fire flooding, electrode original position heating to impel reservoir temperature to rise and reach the purpose of decomposition of hydrate.
Second kind, step-down extraction system; With method mainly is through reducing moving of phase equilibrium line that pressure causes that gas hydrates are stable; Thereby impel gas hydrates to decompose, the free gas under the production of water compound layer is a kind of effective ways that reduce reservoir pressure.
The third, the chemical agent extraction system, mainly be to utilize some chemical agent with method, wait such as salt solution, methyl alcohol, ethanol, ethylene glycol, glycerine to change the phase balance condition that hydrate forms, reduce the hydrate equilibrium temperature, to reach the purpose of decomposition.
Step-down extraction system and the exploitation that heating exploitation method, chemical agent extraction system combine possibly become one of effective ways of large scale mining gas hydrates from now on.And in the reality exploitation, a bite well is far from being enough, and its production efficiency can't improve.
At present, work out gas hydrates effectively, fast, economic mining method, for the large scale mining gas hydrates provide experiment basis and foundation, be the effective way of alleviating the energy pressure that grows with each passing day.
Therefore, prior art awaits to improve and development.
The utility model content
The technical problem that the utility model will solve is; Above-mentioned defective to prior art; The three-dimensional many wells unitized production of a kind of gas hydrates experimental facilities is provided; Provide a kind of can the various withdrawal mechanisms of comprehensive study, production performance and the three-dimensional many wells unitized production of gas hydrates experimental facilities that various exploitation methods are optimized; This experimental facilities is realized the simulation to the many well exploitations of hydrate through experiment, thereby the three-dimensional simulation experiment is expanded, and for making the mode of utilizing many wells unitized production in the reality improve production efficiency experiment basis and foundation is provided.
The technical scheme that the utility model technical solution problem is adopted is following:
The three-dimensional many wells unitized production of a kind of gas hydrates experimental facilities wherein, comprises three-dimensional autoclave, import barrier unit, outlet controlling unit, data processing unit;
Said three-dimensional autoclave is connected with import barrier unit, outlet controlling unit, data processing unit respectively; Sensing element in said import barrier unit, the outlet controlling unit all is connected with data processing unit with data wire through holding wire;
Be the simulation chamber of sealing in the three-dimensional autoclave, simulation is filled with porous media in the chamber, is used to simulate environments such as subsea, and in the simulation chamber, arranges the well pattern that is used for simulation mining;
The import barrier unit is used in three-dimensional autoclave, importing water, natural gas, and the pressure of the natural gas of control input;
Outlet controlling unit is used to control the natural gas after the simulation mining, the output pressure of water;
Data processing unit is used to gather and handle the induced signal of each sensing element;
Wherein, said three-dimensional autoclave is provided with some inner wells in simulation chamber that stretch into, and comprises a central vertical well and some vertical side wells; To simulate the chamber and vertically be divided into n horizontal bedding, each vertical well casing stretches to respectively on the horizontal bedding of the different depth in the simulation chamber.
The three-dimensional many wells unitized production of said gas hydrates experimental facilities wherein, is arranged the pressure sensor and the temperature pick up that change in order to the monitoring recovery process in the said three-dimensional autoclave; Said autoclave places thermostatic chamber, in order to keep stationary temperature;
Comprise the NaOH solution tank NaOH, topping-up pump, the heating tank that connect successively in the said import barrier unit, and the compressed air source unit, the gas flowmeter that connect successively; Solution injects three-dimensional autoclave via NaOH solution tank NaOH, topping-up pump and heating tank successively; Gas injects three-dimensional autoclave via compressed air source unit and gas flowmeter;
Said outlet controlling unit comprises electronic balance, reaches the back-pressure valve, gas-liquid separator, the gas flowmeter that connect successively, and said electronic balance is connected to gas-liquid separator; Natural G&W flows out via back-pressure valve, through gas-liquid separator, is divided into that branch is vented one's spleen and decomposition water, divides and vents one's spleen by the gas flowmeter metering, and decomposition water is measured by electronic balance.
The three-dimensional many wells unitized production of said gas hydrates experimental facilities, wherein, said three-dimensional autoclave comprises kettle and kettle cover plate, fixing seal between kettle cover plate and the kettle; Annular seal space between kettle and the kettle cover plate constitutes said simulation chamber, and the inwall of kettle is the plane wall, constitutes impermeable straight border, and the inwall around the kettle is provided with heat insulation layer.
The three-dimensional many wells unitized production of said gas hydrates experimental facilities, wherein, the peupendicular hole that stretches into simulation chamber set inside is 5 groups or 9 groups;
When being set to 5 groups, wherein 4 groups as vertical side well, be respectively the first vertical side well V1, the 3rd vertical side well V3, the vertical side well of the 7th vertical side well V7 V9 with the 9th, another is organized as the central vertical well, is vertical centre well V5;
When being set to 9 groups; Wherein 8 groups as vertical side wells; Be respectively the first vertical side well V1, the second vertical side well V2, the 3rd vertical side well V3, the 4th vertical side well V4, the straight side well of sextuple V6, the 7th vertical side well V7, the vertical side well with the 9th of the 8th vertical side well V8 V9, another group vertical centre well V5 is as the central vertical well;
Wherein 4 groups or 8 groups of vertical side wells are square profile, and are close to simulation cavity wall face, and as another group of vertical centre well, are located at the centre of vertical side well, promptly simulate the center on the vertical direction of chamber.
The three-dimensional many wells unitized production of said gas hydrates experimental facilities, wherein, said vertical centre well stretches to bottom leveling course, vertical side well stretches to top layer leveling course.
The three-dimensional many wells unitized production of said gas hydrates experimental facilities, wherein, evenly 4 of cuttings on every well casing, length is identical with the thickness of leveling course, in order to simulate the peupendicular hole perforation.
The three-dimensional many wells unitized production of said gas hydrates experimental facilities, wherein, the outer wall of said kettle is square or cylinder, the simulation chamber is a square.
The three-dimensional many wells unitized production of said gas hydrates experimental facilities, wherein, the withstand voltage scope of said three-dimensional autoclave is 0～40MPa; The volume in said simulation chamber is 0.1L～500L.
A kind of three-dimensional simulation experimental technique based on the three-dimensional many wells unitized production of above-mentioned said gas hydrates experimental facilities wherein, comprises step:
Through regulating temperature that the thermostatic chamber temperature control part divides to set the experimental situation temperature;
In three-dimensional autoclave, inject natural G&W through the import barrier unit, controlled pressure, the generative process of simulation gas hydrates;
After natural gas hydrate generates completion, through control import barrier unit and outlet controlling unit, the recovery process of simulation gas hydrates;
Through the natural gas after the outlet controlling unit control simulation mining, the output pressure of water;
And through the data processing unit collection with handle the induced signal of each sensing element,
Wherein, the solution before the simulation mining injects three-dimensional autoclave via NaOH solution tank NaOH, topping-up pump and the heating tank of import barrier unit successively; Gas injects three-dimensional autoclave via the compressed air source unit and the gas flowmeter of import barrier unit;
Natural G&W after the simulation mining flows out via back-pressure valve, through gas-liquid separator, is divided into that branchs vented one's spleen and decomposition water, and dividing vents one's spleen is measured by gas flowmeter, and decomposition water is measured by electronic balance.
Described three-dimensional simulation experimental technique; Wherein, When experiment needs the simulation Five-point method pattern, open the first vertical side well V1 of vertical side well, the 3rd vertical side well V3; The well head of the vertical side well with the 9th of the 7th vertical side well V7 V9 is as the extraction well, with vertical centre well V5 as injecting well;
When experiment needs the simulation seven-spat pattern; The well head of the first vertical side well V1, the second vertical side well V2, the 3rd vertical side well V3, the 7th vertical side well V7, the vertical side well with the 9th of the 8th vertical side well V8 V9 of opening vertical side well is as the extraction well, with vertical centre well V5 as injecting well;
When experiment needs 9 method well patterns of simulation; The well head of the first vertical side well V1, the second vertical side well V2, the 3rd vertical side well V3, the 4th vertical side well V4, the straight side well of sextuple V6, the 7th vertical side well V7, the vertical side well with the 9th of the 8th vertical side well V8 V9 of opening vertical side well is as the extraction well, with vertical centre well V5 as injecting well.
The beneficial effect of the utility model is: the three-dimensional many wells unitized production of the gas hydrates that the utility model provided experimental facilities, can simulate many wells unitized production hydrate; Be applicable to the three-dimensional autoclave of all size; Can let three-dimensional hydrate physical simulating device by the laboratory yardstick that is limited to, be amplified to infinitely great stratum and get on, they can the various withdrawal mechanisms of comprehensive study, production performance and various exploitation methods are optimized and overall merit; For the large scale mining gas hydrates provide experiment basis and foundation.
Description of drawings
Fig. 1 is the three-dimensional many wells unitized production of the gas hydrates experimental facilities structural representation of the utility model embodiment.
Fig. 2 is a three-dimensional agitated reactor interior well arrangement sketch map among Fig. 1.
Fig. 3 is the detailed structure structural representation of three-dimensional agitated reactor interior well among Fig. 2.
The specific embodiment
For the purpose, technical scheme and the advantage that make the utility model is clearer, clear and definite, below develop simultaneously embodiment to the utility model further explain with reference to accompanying drawing.Should be appreciated that specific embodiment described herein only in order to explanation the utility model, and be not used in qualification the utility model.
The physical model experiment purpose is that the actual hydrate of simulation is hidden infinitely great relatively stratum dynamic parameter situation of change; But the experiment agitated reactor has the border to exist; The existence on border all can exert an influence to equipotential lines distribution, streamline distribution and the well yield of seepage field, claims that usually this influence is " boundary effect ".In order to handle " boundary effect " of seepage field, according to the meeting point reaction method of straight line impermeable boundary, minute surface can be used as in the impermeable boundary, and reflection a bite equicohesive virtual producing well on the symmetric position of its opposite side is (if having the border then simultaneously right.Claim reflection border of the same type on the position), seepage field that at this moment forms and border are identical to the seepage field of the influence formation of well, are referred to as " mirrored effect ", have therefore solved the influence of boundary effect to seepage field.
When hydrate three-dimensional experiment physical model need expand in the infinitely great stratum, palpiform becomes impermeable straight border and the adiabatic border of thermal field of the seepage field of wall.
Five-spot pattern method, seven spot pattern method and nine-spot pattern method are the well spacing methods that tradition is used for the recover petroleum natural gas.The five-spot pattern method refers to be injected well and alternately arranges with withdrawal well, and each has four withdrawal wells around injecting well, and four injection wells are arranged around each same withdrawal well, produces notes than being 1: 1; The seven spot pattern method refers to each and injects and six withdrawal wells to be arranged around well but two or four injection wells are arranged around each withdrawal well, produces and annotates than being 2: 1; The nine-spot pattern method refers to each and injects and eight withdrawal wells to be arranged around well but two or four injection wells are arranged around each withdrawal well, produces and annotates than being 3: 1.Because this experimental temperature fringe conditions can be thought adiabatic fringe conditions, the seepage field fringe conditions is the straight line impermeable boundary.Can satisfy to expand in the infinitely great stratum according to the well pattern setting of " mirrored effect " this experiment on border and go, meet five-spot in the infinitely great stratum, 7 methods and 9 rules that the method well pattern is arranged.
Because the particularity of the exploitation of methane hydrate, well to pierce the degree of depth inequality, inject well and need pierce hydrate and hide bottom, hide the decomposition water compound in order to the heating hydrate; Recovery well only need pierce hydrate Tibetan top layer and get final product, because the methane gas that decomposition of hydrate produces moves upward, what recovery well brought to Front and helps exploiting carries out.
The purpose of the utility model just provides the three-dimensional many wells unitized production of a kind of gas hydrates experimental facilities, and this experimental facilities is realized the simulation to the many well exploitations of hydrate through experiment, thereby the three-dimensional simulation experiment is expanded.
As shown in Figure 1, the three-dimensional many wells unitized production of a kind of gas hydrates of the utility model embodiment experimental facilities comprises three-dimensional autoclave 3, import barrier unit 200, outlet controlling unit 300, data processing unit 400.Said three-dimensional autoclave 3 is connected with import barrier unit 200, outlet controlling unit 300, data processing unit 400 respectively; Sensing element in said import barrier unit 200, the outlet controlling unit 300 all is connected with data processing unit 400 with data wire through holding wire.
As shown in Figure 1; Import barrier unit 200 is used for input water, natural gas in three-dimensional autoclave 3; And the pressure of the natural gas of control input; This import barrier unit 200 comprises NaOH solution tank NaOH 8, topping-up pump 9, the heating tank 10 that connects successively, and the compressed air source unit 1, the gas flowmeter 2 that connect successively.Gas injects three-dimensional autoclave 3 via compressed air source unit 1 and gas flowmeter 2, and solution is via NaOH solution tank NaOH 8, and topping-up pump 9 injects three-dimensional autoclave 3 with heating tank 10.
Wherein, said three-dimensional autoclave 3 comprises kettle and kettle cover plate, fixing seal between kettle cover plate and the kettle; Annular seal space between kettle and the kettle cover plate constitutes said simulation chamber 101, and the inwall of kettle is the plane wall, constitutes impermeable straight border, and the inwall around the kettle is provided with heat insulation layer.Preferably, the outer wall of said kettle is square or cylinder, and the simulation chamber is a square.
Among the utility model embodiment, three-dimensional autoclave 3, import barrier unit 200, outlet controlling unit 300, data processing unit 400 all adopt existing three-dimensional hydrate exploitation physical simulation techniques, below specify the many wells well spacing in the three-dimensional autoclave.
Adopting the withstand voltage scope of said three-dimensional autoclave in the present embodiment is 0～40MPa; The volume in said simulation chamber is 0.1L～500L.
See also Fig. 2, three-dimensional autoclave 3 is provided with some wells that stretch into 101 inside, simulation chamber, comprises a central vertical well and some vertical side wells.To simulate the chamber and vertically be divided into n horizontal bedding; Preferred 4 layers, as shown in Figure 2 begins from top layer 102, and 102 to A-A layers are first floor H1; The A-A layer is second layer H2 to the B-B layer; The B-B layer is the 3rd layer of H3 to the C-C layer, and the C-C layer is the 4th layer of H4 to bottom 103, and the vertical well casing of each root stretches to respectively on the horizontal bedding of the different depth in the simulation chamber.
Stretch into the inner peupendicular holes in simulation chamber 101 5 groups or 9 groups (preferred 9 groups) are arranged: under 9 groups situation; Wherein 8 groups as vertical side wells; Be respectively the first vertical side well V1, the second vertical side well V2, the 3rd vertical side well V3, the 4th vertical side well V4, the straight side well of sextuple V6, the 7th vertical side well V7, the vertical side well with the 9th of the 8th vertical side well V8 V9, another group vertical centre well V5 is as the central vertical well.
When being set to 5 groups, wherein 4 groups as vertical side well, be respectively the first vertical side well V1, the 3rd vertical side well V3, the vertical side well of the 7th vertical side well V7 V9 with the 9th, another is organized as the central vertical well, is vertical centre well V5.
4 groups or 8 groups of vertical side wells are square profile, and are close to threedimensional model simulation cavity wall face (when the inwall side in the simulation chamber was provided with thermal insulation slab, each was organized vertical side well and is close to thermal insulation slab).And remaining 1 group (V5 as shown in Figure 2) is located at the centre of vertical side well as the vertical centre well, promptly simulates the center on the vertical direction of chamber.
Wherein, vertical centre well 23 stretches to the bottom 103 leveling courses, and vertical side well (19,20,21,22,24,25,26,27) stretches to the A-A layer of top leveling course.
On the borehole wall of every well casing 100, evenly be carved with groove 104 in the utility model, embodiment as shown in Figure 3 is advancing to be carved with on the wall 4 grooves 104, and length is identical with the thickness of leveling course, in order to simulation peupendicular hole perforation.
Below the operating principle of the three-dimensional many wells associating experimental facilitiess of the gas hydrates of the utility model embodiment is elaborated:
When adopting the three-dimensional many wells associating experimental facilitiess of above-mentioned gas hydrates to carry out three-dimensional many well simulation experiments, as shown in Figure 1, through regulating thermostatic chamber 5 to set the experimental situation temperature; Inject natural G&W through import barrier unit 200, controlled pressure, the generative process of simulation gas hydrates; After natural gas hydrate generates completion, through control import barrier unit 200 and outlet controlling unit 300, the recovery process of simulation gas hydrates; After accomplishing, experiment passes through data processing unit 400 deal with data.
Based on the foregoing description, the utility model embodiment also provides a kind of three-dimensional simulation experimental technique based on the three-dimensional many wells unitized production of above-mentioned said gas hydrates experimental facilities, mainly may further comprise the steps:
Through regulating temperature that the thermostatic chamber temperature control part divides to set the experimental situation temperature;
In three-dimensional autoclave, inject natural G&W through the import barrier unit, controlled pressure, the generative process of simulation gas hydrates;
After natural gas hydrate generates completion, through control import barrier unit and outlet controlling unit, the recovery process of simulation gas hydrates;
Through the natural gas after the outlet controlling unit control simulation mining, the output pressure of water;
And through the data processing unit collection with handle the induced signal of each sensing element,
Wherein, the solution before the simulation mining injects three-dimensional autoclave via NaOH solution tank NaOH, topping-up pump and the heating tank of import barrier unit successively; Gas injects three-dimensional autoclave via the compressed air source unit and the gas flowmeter of import barrier unit;
Natural G&W after the simulation mining flows out via back-pressure valve, through gas-liquid separator, is divided into that branchs vented one's spleen and decomposition water, and dividing vents one's spleen is measured by gas flowmeter, and decomposition water is measured by electronic balance, specifically as stated.
As shown in Figure 3, said three-dimensional simulation experimental technique wherein, when experiment needs the simulation Five-point method pattern, is opened the V1 19 of vertical side well, and V3 21, and V7 25 and V9 27 well heads are as the extraction well, with vertical centre well V5 23 as the injection well; When experiment needs the simulation seven-spat pattern, open the V1 19 of vertical side well, V2 20, V3 21, V7 25, V8 26 and V9 27 well heads are as the extraction well, with vertical centre well V5 23 as the injection well; When experiment needs 9 method well patterns of simulation, open the V1 19 of vertical side well, V2 20, V3 21, V4 22, V6 24, V7 25, V8 26 and V9 27 well heads are as the extraction well, with vertical centre well V5 23 as the injection well.
Through control import barrier unit 200 and outlet controlling unit 300, the recovery process of simulation gas hydrates.After accomplishing, experiment passes through data processing unit 400 deal with data.
In sum, three-dimensional many wells unitized production experimental facilities of the gas hydrates that the utility model provided and experimental technique thereof can be simulated many wells unitized production hydrate; Be applicable to the three-dimensional autoclave of all size; Can let three-dimensional hydrate physical simulating device by the laboratory yardstick that is limited to, be amplified to infinitely great stratum and get on, they can the various withdrawal mechanisms of comprehensive study, production performance and various exploitation methods are optimized and overall merit; For the large scale mining gas hydrates provide experiment basis and foundation.
Should be understood that; The application of the utility model is not limited to above-mentioned giving an example; Concerning those of ordinary skills, can improve or conversion according to above-mentioned explanation, all these improvement and conversion all should belong to the protection domain of the utility model accompanying claims.
Claims (8)
1. the three-dimensional many wells unitized production of a gas hydrates experimental facilities is characterized in that, comprises three-dimensional autoclave, import barrier unit, outlet controlling unit, data processing unit;
Said three-dimensional autoclave is connected with import barrier unit, outlet controlling unit, data processing unit respectively; Sensing element in said import barrier unit, the outlet controlling unit all is connected with data processing unit with data wire through holding wire;
Be the simulation chamber of sealing in the three-dimensional autoclave, simulation is filled with porous media in the chamber, is used to simulate environments such as subsea, and in the simulation chamber, arranges the well pattern that is used for simulation mining;
The import barrier unit is used in three-dimensional autoclave, importing water, natural gas, and the pressure of the natural gas of control input;
Outlet controlling unit is used to control the natural gas after the simulation mining, the output pressure of water;
Data processing unit is used to gather and handle the induced signal of each sensing element;
Wherein, said three-dimensional autoclave is provided with some inner wells in simulation chamber that stretch into, and comprises a central vertical well and some vertical side wells; To simulate the chamber and vertically be divided into n horizontal bedding, each vertical well casing stretches to respectively on the horizontal bedding of the different depth in the simulation chamber.
2. according to the three-dimensional many wells unitized production of the said gas hydrates of claim 1 experimental facilities, it is characterized in that, arrange the pressure sensor and the temperature pick up that change in order to the monitoring recovery process in the said three-dimensional autoclave; Said autoclave places thermostatic chamber, in order to keep stationary temperature;
Comprise the NaOH solution tank NaOH, topping-up pump, the heating tank that connect successively in the said import barrier unit, and the compressed air source unit, the gas flowmeter that connect successively; Solution injects three-dimensional autoclave via NaOH solution tank NaOH, topping-up pump and heating tank successively; Gas injects three-dimensional autoclave via compressed air source unit and gas flowmeter;
Said outlet controlling unit comprises electronic balance, reaches the back-pressure valve, gas-liquid separator, the gas flowmeter that connect successively, and said electronic balance is connected to gas-liquid separator; Natural G&W flows out via back-pressure valve, through gas-liquid separator, is divided into that branch is vented one's spleen and decomposition water, divides and vents one's spleen by the gas flowmeter metering, and decomposition water is measured by electronic balance.
3. according to the three-dimensional many wells unitized production of the said gas hydrates of claim 1 experimental facilities, it is characterized in that said three-dimensional autoclave comprises kettle and kettle cover plate, fixing seal between kettle cover plate and the kettle; Annular seal space between kettle and the kettle cover plate constitutes said simulation chamber, and the inwall of kettle is the plane wall, constitutes impermeable straight border, is provided with heat insulation layer around the kettle.
4. according to the three-dimensional many wells unitized production of the said gas hydrates of claim 1 experimental facilities, it is characterized in that the peupendicular hole that stretches into simulation chamber set inside is 5 groups or 9 groups;
When being set to 5 groups, wherein 4 groups as vertical side well, be respectively the first vertical side well (V1), the 3rd vertical side well (V3), the 7th vertical side well of vertical side well (V7) (V9) with the 9th, another is organized as the central vertical well, is vertical centre well (V5);
When being set to 9 groups; Wherein 8 groups as vertical side wells; Be respectively the first vertical side well (V1), the second vertical side well (V2), the 3rd vertical side well (V3), the 4th vertical side well (V4), the straight side well of sextuple (V6), the 7th vertical side well (V7), the 8th vertical side well with the 9th of vertical side well (V8) (V9), another group vertical centre well (V5) is as the central vertical well;
Wherein 4 groups or 8 groups of vertical side wells are square profile, and are close to simulation cavity wall face, and as another group of vertical centre well, are located at the centre of vertical side well, promptly simulate the center on the vertical direction of chamber.
5. according to the three-dimensional many wells unitized production of the said gas hydrates of claim 1 experimental facilities, it is characterized in that said vertical centre well stretches to bottom leveling course, vertical side well stretches to top layer leveling course.
6. according to the three-dimensional many wells unitized production of the said gas hydrates of claim 1 experimental facilities, it is characterized in that even cutting is 4 on the every well casing, length is identical with the thickness of leveling course, in order to simulation peupendicular hole perforation.
7. according to the three-dimensional many wells unitized production of the said gas hydrates of claim 1 experimental facilities, it is characterized in that the outer wall of said kettle is square or cylinder, the simulation chamber is a square.
8. according to the three-dimensional many wells unitized production of the said gas hydrates of claim 1 experimental facilities, it is characterized in that the withstand voltage scope of said three-dimensional autoclave is 0～40MPa; The volume in said simulation chamber is 0.1L～500L.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102305052A (en) * | 2011-09-05 | 2012-01-04 | 中国科学院广州能源研究所 | Three-dimensional multiwall combined exploration experimental apparatus for natural gas hydrate and experimental method thereof |
| CN104616579A (en) * | 2015-01-08 | 2015-05-13 | 西南石油大学 | Gas production simulation system and simulation method |
| CN105301200A (en) * | 2015-11-12 | 2016-02-03 | 中国科学院广州能源研究所 | Testing apparatus for characteristics of sand production during mining of natural gas hydrate |
| CN105443090A (en) * | 2015-12-28 | 2016-03-30 | 中国石油天然气股份有限公司 | Experimental device and method for measuring influence of water injection and gas injection on oil reservoir development |
| CN111948370A (en) * | 2020-08-06 | 2020-11-17 | 中国科学院广州能源研究所 | Flow field measuring device and measuring method for natural gas hydrate experiment system |
| CN112083124A (en) * | 2020-08-06 | 2020-12-15 | 中国科学院广州能源研究所 | Physical property characterization device and method in natural gas hydrate large-scale experiment system |
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2011
- 2011-09-05 CN CN2011203316224U patent/CN202220587U/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102305052A (en) * | 2011-09-05 | 2012-01-04 | 中国科学院广州能源研究所 | Three-dimensional multiwall combined exploration experimental apparatus for natural gas hydrate and experimental method thereof |
| CN104616579A (en) * | 2015-01-08 | 2015-05-13 | 西南石油大学 | Gas production simulation system and simulation method |
| CN105301200A (en) * | 2015-11-12 | 2016-02-03 | 中国科学院广州能源研究所 | Testing apparatus for characteristics of sand production during mining of natural gas hydrate |
| CN105443090A (en) * | 2015-12-28 | 2016-03-30 | 中国石油天然气股份有限公司 | Experimental device and method for measuring influence of water injection and gas injection on oil reservoir development |
| CN105443090B (en) * | 2015-12-28 | 2018-12-25 | 中国石油天然气股份有限公司 | Experimental device and method for measuring influence of water injection and gas injection on oil reservoir development |
| CN111948370A (en) * | 2020-08-06 | 2020-11-17 | 中国科学院广州能源研究所 | Flow field measuring device and measuring method for natural gas hydrate experiment system |
| CN112083124A (en) * | 2020-08-06 | 2020-12-15 | 中国科学院广州能源研究所 | Physical property characterization device and method in natural gas hydrate large-scale experiment system |
| CN112083124B (en) * | 2020-08-06 | 2021-08-17 | 中国科学院广州能源研究所 | Physical property characterization device and method in natural gas hydrate large-scale experiment system |
| WO2021159696A1 (en) * | 2020-08-06 | 2021-08-19 | 中国科学院广州能源研究所 | Reduced scale natural gas hydrate reservoir physical characteristics representation apparatus and method |
| US11566493B2 (en) | 2020-08-06 | 2023-01-31 | Guangzhou Institute Of Energy Conversion, Chinese Academy Of Sciences | Physical characterization device and method for scale model of natural gas hydrate reservoir |
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