CN209483311U - The pressure test device of fluid jet in-situ retorting gas hydrates - Google Patents
The pressure test device of fluid jet in-situ retorting gas hydrates Download PDFInfo
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- CN209483311U CN209483311U CN201920092653.5U CN201920092653U CN209483311U CN 209483311 U CN209483311 U CN 209483311U CN 201920092653 U CN201920092653 U CN 201920092653U CN 209483311 U CN209483311 U CN 209483311U
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Abstract
The pressure test device of fluid jet in-situ retorting gas hydrates, it is related to ocean gas hydrate development field, device includes injected system, jet crushing system, ring pressure system, axis pressure system, back pressure system, vacuum system, simulation system, acquisition processing system and metering system, by the pipe valve on control piper, each system can independent operating；The confining pressure load of device is pressed independently of axis to be loaded, noiseless between each other；Simultaneously, the jet break process of the object containing natural gas hydrate deposits can be observed in real time by video camera, the device of the utility model with the simulated sea bottom true confining pressure containing natural gas hydrate stratum in situ, axis press strip part and can flood environment, true and reliable data are provided, provide theory support for the exploitation of ocean gas hydrate.
Description
Technical field
The utility model relates to ocean gas hydrate development field, in particular to a kind of fluid jet in-situ retorting is natural
The pressure test device of gas hydrate.
Background technique
Gas hydrates (Natural Gas Hydrates, abbreviation NGH) are under certain condition by lighter hydrocarbons, titanium dioxide
The white solid state crystalline material that the micro-molecular gas such as carbon and hydrogen sulfide and water phase interaction are formed has energy density big, certain
Formation condition, reserves are big and wide four main features of distribution.The total organic carbon contained in the gas hydrates in the whole world is suitable
In 2 times of explored conventional fossil carbon reserves.Since the resource potential of gas hydrates is huge, recent decades are alive
Risen within the scope of boundary gas hydrates reconnoitre, the research boom of pilot production, exploitation, the U.S., Japan, Canada, India and Korea Spro
Guo Deng state has formulated the plan of studying for a long period of time for gas hydrates, how to exploit safe and efficiently and environmentally friendly natural
Gas hydrate resource has become forward position and the focus of countries in the world concern.
Conventional natural gas exploiting method has temperature activation method, voltage drop method, note chemical-agent technique and CO at present2Displacement method；And
Compared with conventional gas and oil reservoir, ocean gas hydrate reservoir has the characteristics that shallow buried depth, non-diagenesis and hyposmosis；Therefore,
If merely developing using these four recovery methods to ocean gas hydrate, there is biggish limitation: voltage drop method
It may cause the secondary generation of gas hydrates or the generation of ice, block permeation pathway, it is unfavorable in exploiting for a long time；Heat shock method
With the lower problem of efficiency of heating- utilization, and small range heating can only be carried out；The shortcomings that chemical-agent technique is chemical reagent valuableness,
Slow to the effect of gas hydrates layer, there are problem of environmental pollutions；CO2It is long that displacement method exploits the period, it is desirable that gas water
Close object reservoir permeability with higher.
It is exploiting ocean natural gas hydrates new method, water jet that water jet erosion, which is crushed sea bed gas hydrate reservoir,
The method feature shallower lower than deep-sea oil gas reservoir, covered depth using gas hydrates reservoir mechanical strength, it is broken using jet stream
Broken mode do not need huge energy input just and can produce it is broken, to obtain gas hydrate particle；In addition to this, water-jet
Stream method is not required to make the gas hydrate dissociation in reservoir by pressure or temperature transmitting, does not have to the heat transfer of reservoir, pressure transmission channel
It requires, therefore tonicity requirements are low；Water jet method is not caused Temperature-pressure Conditions to change by gas hydrate dissociation simultaneously, thus
Generate the influence that secondary gas hydrates hinder reaction to carry out；This method has widely applicable model compared to other methods
It encloses, is considered as the recovery method of preferable prospect；Therefore, it anticipates to the research of jet crushing gas hydrates principle and rule
Justice is great.
The seabed preservation of object containing natural gas hydrate deposits is crushed gas hydrates in hyperbaric environment, carrying out water jet method
When experiment, to simulate subsea environment in situ, guarantee that the confining pressure of the object containing natural gas hydrate deposits and axis pressure load are most important；If
The actual high-voltage occurrence condition of the object containing natural gas hydrate deposits, will lead to penetrating of being studied when being unable to satisfy jet crushing experiment
Flow the inaccuracy of the broken principle of object containing natural gas hydrate deposits and rule.
Utility model content
The purpose of the utility model is to provide a kind of pressure test device of fluid jet in-situ retorting gas hydrates,
All be distributed with pipe valve in each system for including in the device, each system can independent operating, it is highly-safe.
The pressure test device of fluid jet in-situ retorting gas hydrates provided by the utility model, which is characterized in that
The device includes: injected system, jet crushing system, ring pressure system, axis pressure system, back pressure system, vacuum system, simulation system
System, acquisition processing system and metering system；
The injected system, axis pressure system and vacuum system are connected by the air inlet of admission line and triple valve, simultaneously
Two gas outlets of triple valve pass through gas injecting pipe respectively, axis pressure pipeline is connected to simulation system, and is arranged on gas injecting pipe
There are pressure sensor I and pipe valve I, injected system is for methane of the injection for synthesis of natural gas hydrate into simulation system
Gas, and make methane gas be pressurized to meet synthesis of natural gas hydrate needed for pressure condition, injected system includes methane gas
Bottle, pressure reducing valve, pipe valve II, pressure regulator valve I, booster pump, air compressor machine, buffer container, gas flow control meter, check valve and pipe valve
Part III, the methane gas cylinder is by the first piping connection to admission line, in being sequentially arranged pressure reducing valve, pipe on the first pipeline
Valve member II, pressure regulator valve I, gas flow control meter, check valve and pipe valve III；The inlet end of the booster pump passes through the second pipeline
It is connect with air compressor machine, and is provided with pressure regulator valve II on the second pipeline, the outlet side of booster pump passes through third pipeline and respectively
In four piping connections to the first pipeline, the junction of third pipeline and the first pipeline is between pressure reducing valve and pipe valve II, together
When third pipeline on be provided with pipe valve IV, the junction of the 4th pipeline and the first pipeline be located at pipe valve II and pressure regulator valve I it
Between, in being provided with pipe valve V and pipe valve VI on the 4th pipeline；Pressure gauge is provided on the buffer container, buffer container is logical
Cross the 5th pipeline and the 4th piping connection, and the junction of the 5th pipeline and the 4th pipeline be located at pipe valve V and pipe valve VI it
Between；
The jet crushing system is connected to by jet pipe with simulation system, and jet crushing system is used to spray to simulation system
The high pressure water flow of established natural gas hydrate deposits object inside broken simulation system is penetrated, jet crushing system includes jet stream
Pump, jet pipe, jet nozzle and elevating mechanism, jet pump are connect with jet pipe, and are provided between jet pump and jet pipe
Pipe valve VII；The visual test cabin top that jet pipe passes through simulation system extends to inside it, and jet pipe is fixed on elevating mechanism
On, the jet stream end of jet pipe is equipped with jet nozzle；
The ring pressure system is connected to the ring pressure hole being arranged on visual test cabin, and ring presses system to be used for simulation system
System provides the confining pressure of sea bed gas hydrate sedimentary original position；Ring pressure system includes ring press pump and ring moulding set, and ring press pump is logical
It crosses pipeline to be connected to ring moulding set, pressure sensor II and pipe valve VIII is provided on the pipeline；The ring moulding set setting
Inside visual test cabin, sealing strip and sealing ring are provided in the gap between ring moulding set and drive end bearing bracket, visual window；
The axis pressure system is connected to simulation system, and axis presses system to be used to provide sea-bottom natural gas water to the simulation system
Close the axis pressure of object sedimentary original position；Axis pressure system includes constant-flux pump, axis pressure pipeline, axis pressure loading chamber, loading axis and pressure plare, institute
It states constant-flux pump to pass through in the 6th piping connection to admission line, and is provided with pipe valve Ⅸ on the 6th pipeline；The axis pressure pipe
Road is connected to the axis pressure loading chamber being arranged in inside rear end cap；Loading axis one end setting is inside axis pressure loading chamber, load
The other end of axis is extended to inside visual test cabin warehouse across rear end cap and is connect with pressure plare；The pressure plare and ring moulding set
Between, between loading axis and ring moulding set, at the gap between loading axis and rear end cap and between axis pressure loading chamber and rear end cap
It is provided with sealing strip and sealing ring；
The back pressure system includes gas-guide tube, back-pressure valve, backpressure pump and back pressure buffer container, one end of gas-guide tube and jet stream
Pipe connection, the other end of gas-guide tube are connected to back pressure buffer container, and back-pressure valve, pipe valve Ⅹ and pressure are provided on gas-guide tube
Sensor III, the back pressure buffer container is connected to backpressure pump, and is provided with pipe valve between back pressure buffer container and backpressure pump
Part Ⅺ；
The vacuum system includes vacuum meter, vacuum tank and vacuum pump, and one end of vacuum tank is controlled to a vacuum pump, very
The other end of empty container is by the 7th piping connection to admission line, in being disposed with pipe valve Ⅻ, peace on the 7th pipeline
Full valve and pressure sensor IV, the vacuum meter are arranged on vacuum tank；
The acquisition processing system includes pressure sensor I, pressure sensor II, pressure sensor III, pressure sensor
IV, temperature sensor and controlling terminal, pressure sensor I, pressure sensor II, pressure sensor III, pressure sensor IV and
Temperature sensor is communicated to connect with controlling terminal；
The metering system includes drier, three phase separator and minimum gas metering device, the three phase separator with
Gas-guide tube connection, the top outlet side of three phase separator is connected to minimum gas metering device, and three phase separator with it is micro
Drier is provided between gas-metering device；
The simulation system includes insulating box, visual test cabin, turning supporting seat and video camera, and the turning supporting seat setting exists
The inner top of insulating box；The visual test cabin is mounted in turning supporting seat, and visual test cabin includes visual test cabin warehouse, preceding
End cap and rear end cap, the drive end bearing bracket are fastened on the front end of visual test cabin warehouse by sealing valve, and are arranged on drive end bearing bracket
There is visual window；The rear end cap is fastened on the rear end of visual test cabin warehouse by sealing valve；The video camera is placed in visual examination
Outside testing position, and its face visual window is arranged.
The jet crushing system is 20mm at a distance from visual window.
The piston stroke of the loading axis is 30mm.
The quantity of the temperature sensor is three, and three temperature sensors are arranged on the side wall of visual test cabin.
Through the above design, the utility model can be brought the following benefits: jet stream provided by the utility model
The pressure test device of method in-situ retorting gas hydrates, each system for including in device can independent operating.In order to
It is safe, pipe valve is distributed in each system.The axis pressure loading direction and visual window of the object containing natural gas hydrate deposits are arranged
Direction is consistent, and axis pressure load uses dual-seal to prevent from leaking；Confining pressure loading direction is vertical with visual window arranged direction, and
Confining pressure load is pressed independently of axis to be loaded, noiseless between each other；Meanwhile it can be observed by video camera and be hydrated containing natural gas in real time
The jet break process of sediment, can be with the simulated sea bottom true confining pressure in situ containing natural gas hydrate stratum, axis press strip part
With flood environment, true and reliable data are provided, provide theory support for the exploitation of ocean gas hydrate.
Detailed description of the invention
Attached drawing described herein is used to provide a further understanding of the present invention, and is constituted part of this application,
The utility model illustrative embodiments and their description do not constitute the improper limit of the utility model for understanding the utility model
It is fixed, in the accompanying drawings:
Fig. 1 is the structural schematic diagram of the pressure test device of the utility model fluid jet in-situ retorting gas hydrates.
Fig. 2 is the front view of visual test cabin in the utility model.
Fig. 3 is the side view of visual test cabin in the utility model.
Fig. 4 is video camera schematic diagram in the utility model.
It is respectively marked in figure as follows: 1- methane gas cylinder, 2- pressure reducing valve, 301- pressure regulator valve I, 302- pressure regulator valve II, 401- pipe valve
Part I, 402- pipe valve II, 403- pipe valve III, 404- pipe valve IV, 405- pipe valve V, 406- pipe valve VI, 407- pipe valve
Part VII, 408- pipe valve VIII, 409- pipe valve Ⅸ, 410- pipe valve Ⅹ, 411- pipe valve Ⅺ, 412- pipe valve Ⅻ, 5- pressurization
Pump, 6- controlling terminal, 7- air compressor machine, 8- vacuum pump, 9- buffer container, 10- back pressure buffer container, the control of 11- gas flow
Meter, 12- check valve, 13- constant-flux pump, 14- vacuum meter, 15- pressure gauge, 16- vacuum tank, 17- triple valve, 1801- pressure pass
Sensor I, 1802- pressure sensor II, 1803- pressure sensor III, 1804- pressure sensor IV, 19- safety valve, 20- are penetrated
Flow pump, 21- back-pressure valve, 22- backpressure pump, 23- drier, 24- three phase separator, 25- insulating box, 26- minimum gas metering dress
Set, 27- ring press pump, the visual test cabin of 28-, 29- temperature sensor, 30- elevating mechanism, 31- jet pipe, 32- jet nozzle,
33- ring moulding set, 34- gas injecting pipe, 35- axis pressure loading chamber, 36- rear end cap, 37- axis pressure pipeline, 38- ring pressure hole, 39- add
Carry axis, 40- sealing strip, 41- sealing ring, 42- pressure plare, 43- visual window, 44- sealing valve, 45- turning supporting seat, the front end 46-
Lid, 47- video camera.
Specific embodiment
In order to illustrate more clearly of the utility model, the utility model is done into one below with reference to preferred embodiments and drawings
The explanation of step.It will be appreciated by those skilled in the art that specifically described content is illustrative and be not restrictive below, no
It should limit the protection scope of the present invention.
As shown in Figure 1, Figure 2, shown in Fig. 3 and Fig. 4, fluid jet in-situ retorting gas hydrates described in the present embodiment adds
Compression testing device, the device include injected system, jet crushing system, ring pressure system, axis pressure system, back pressure system, vacuum system
System, simulation system, acquisition processing system and metering system,
The injected system, axis pressure system and vacuum system are connect by admission line with the air inlet of triple valve 17, together
When triple valve 17 two gas outlets pass through gas injecting pipe 34 respectively, axis pressure pipeline 37 is connected to simulation system, and in air injection pipe
Pressure sensor I 1801 and pipe valve I 401 are provided on road 34, injected system is used to inject into simulation system for synthesizing
The methane gas of gas hydrates, and make methane gas be pressurized to meet synthesis of natural gas hydrate needed for pressure condition,
Injected system includes methane gas cylinder 1, pressure reducing valve 2, pipe valve II 402, pressure regulator valve I 301, booster pump 5, air compressor machine 7, buffering appearance
Device 9, gas flow control meter 11, check valve 12 and pipe valve III 403, the methane gas cylinder 1 by the first piping connection into
In feed channel, meter is controlled in being sequentially arranged pressure reducing valve 2, pipe valve II 402, pressure regulator valve I 301, gas flow on the first pipeline
11, check valve 12 and pipe valve III 403；The inlet end of the booster pump 5 is connect by the second pipeline with air compressor machine 7, and the
Pressure regulator valve II 302 is provided on two pipelines, the outlet side of booster pump 5 passes through third pipeline and the 4th piping connection to first respectively
On pipeline, the junction of third pipeline and the first pipeline is between pressure reducing valve 2 and pipe valve II 402, while on third pipeline
Be provided with pipe valve IV 404, the junction of the 4th pipeline and the first pipeline between pipe valve II 402 and pressure regulator valve I 301,
In being provided with pipe valve V 405 and pipe valve VI 406 on the 4th pipeline；It is provided with pressure gauge 15 on the buffer container 9, buffers
Container 9 by the 5th pipeline and the 4th piping connection, and the junction of the 5th pipeline and the 4th pipeline be located at pipe valve V 405 and
Between pipe valve VI 406；The methane purity stored in methane gas cylinder 1 is 99.99%, is used for synthesis of natural gas hydrate；Pressure regulation
Valve I 301 is used to adjust the pressure of methane gas injection, entrance maximum pressure 20MPa；12 pressure resistance 16MPa of check valve, prevents first
Alkane gas backstreaming.Methane gas cylinder 1 releases methane gas, and methane gas output pressure is determined by pressure reducing valve 2, works as output pressure
When insufficient, adjust pressure by pressure regulator valve I 301, booster pump 5 and buffer container 9, after the completion of pressure is adjusted, methane gas according to
It is secondary to be injected in simulation system via triple valve 17, gas injecting pipe 34.
The jet crushing system is connected to by jet pipe 31 with simulation system, jet crushing system and visual window 43
Distance is 20mm, facilitates observation jet break process；Jet crushing system is used to spray in broken simulation system to simulation system
The high pressure water flow of the established natural gas hydrate deposits object in portion, jet crushing system include jet pump 20, jet pipe 31, jet stream
Nozzle 32 and elevating mechanism 30, jet pump 20 connect with jet pipe 31, and are provided with pipe between jet pump 20 and jet pipe 31
Valve member VII 407；Jet pipe 31 extends to inside it at the top of the visual test cabin 28 of simulation system, and jet pipe 31 is fixed on liter
On descending mechanism 30, the jet stream end of jet pipe 31 is equipped with jet nozzle 32, and jet pump 20 is broken natural gas hydrate deposits object
Steady and sustained high pressure water flow, maximum pressure 50Mpa are provided, speed is up to 100m/s；With different jet nozzles 32 come
Simulate different-diameter, shape influences the crushing effect of the object containing natural gas hydrate deposits；Elevating mechanism 30 is for adjusting jet stream
Distance between nozzle 32 and natural gas hydrate deposits object.
The ring pressure system is connected to the ring pressure hole 38 being arranged on visual test cabin 28, and ring presses system to be used for the mould
Quasi- system provides the confining pressure of sea bed gas hydrate sedimentary original position；Ring pressure system includes that ring press pump 27 and ring moulding cover 33,
Ring press pump 27 is connected to by pipeline with ring moulding set 33, and pressure sensor II 1802 and pipe valve VIII are provided on the pipeline
408；The ring moulding set 33 is arranged inside visual test cabin 28, between ring moulding set 33 and drive end bearing bracket 46, visual window 43
It is provided with sealing strip 40 and sealing ring 41 in gap, double-layer seal is formed by sealing strip 40 and sealing ring 41, makes entire ring pressure
System is in sealing state, will not generate gas leak phenomenon；The maximum working pressure (MWP) of ring press pump 27 is 30Mpa, utilizes ring press pump 27
Ring pressure load is carried out to natural gas hydrate deposits object, simulates the true stratum of object containing natural gas hydrate deposits, true reflection is deposited
The natural gas hydrate deposits principle condition of confining pressure on stratum；
The axis pressure system is connected to simulation system, and axis presses system to be used to provide sea-bottom natural gas water to the simulation system
Close the axis pressure of object sedimentary original position；Axis pressure system include constant-flux pump 13, axis pressure pipeline 37, axis pressure loading chamber 35, loading axis 39 and
Pressure plare 42, the constant-flux pump 13 passes through in the 6th piping connection to admission line, and is provided with pipe valve on the 6th pipeline
Ⅸ409；The axis pressure pipeline 37 is connected to the axis pressure loading chamber 35 being arranged in inside rear end cap 36；Described 39 one end of loading axis
Setting inside axis pressure loading chamber 35, the other end of loading axis 39 pass through rear end cap 36 extend to inside visual test cabin warehouse with
Pressure plare 42 connects, and the piston stroke of loading axis 39 is 30mm；Axis presses system and ring pressure system independent mutually, can individually give
Pressure, the triaxial pressure state of real simulation seabed object containing natural gas hydrate deposits；The pressure plare 42 and ring moulding set 33
Between, between loading axis 39 and ring moulding set 33, between loading axis 39 and rear end cap 36 and axis pressure loading chamber 35 and rear end cap 36
Between gap at be provided with sealing strip 40 and sealing ring 41；The double-layer seal that sealing strip 40 and sealing ring 41 are formed, makes whole
A axis pressure system is in sealing state；The maximum working pressure (MWP) of constant-flux pump 13 is 50Mpa, provides pressure using constant-flux pump 13, uses
To simulate axis pressure condition suffered by natural gas hydrate deposits object.
The back pressure system includes gas-guide tube, back-pressure valve 21, backpressure pump 22 and back pressure buffer container 10, one end of gas-guide tube
It is connected to jet pipe 31, the other end of gas-guide tube is connected to back pressure buffer container 10, and back-pressure valve 21, pipe are provided on gas-guide tube
Valve member Ⅹ 410 and pressure sensor III 1803, the back pressure buffer container 10 are connected to backpressure pump 22, and in back pressure buffer container
Pipe valve Ⅺ 411 is provided between 10 and backpressure pump 22, the operating pressure of backpressure pump 22 is between 0~50MPa；Due to visually trying
Pressure inside testing position 28 is big, and rate of discharge is high, and air pressure fluctuation is big, fluid can be made steady by back pressure system, be easy to test.
The vacuum system includes vacuum meter 14, vacuum tank 16 and vacuum pump 8, one end of vacuum tank 16 and vacuum pump
8 connections, the other end of vacuum tank 16 is by the 7th piping connection to admission line, in being disposed with pipe on the 7th pipeline
Valve member Ⅻ 412, safety valve 19 and pressure sensor IV 1804, the vacuum meter 14 are arranged on vacuum tank 16；The vacuum
The vacuum degree of pump 8 is 0.1Pa, and vacuum tank 16 is used to store the gas extracted out from simulation system, and vacuum meter 14 is used to indicate gas
Body storage capacity after natural gas hydrate deposits object has synthesized, carries out vacuum pumping to visual test cabin 28, guarantees experiment
Accuracy.
The acquisition processing system includes pressure sensor I 1801, pressure sensor II 1802, pressure sensor III
1803, pressure sensor IV 1804, temperature sensor 29 and controlling terminal 6, pressure sensor I 1801, pressure sensor II
1802, pressure sensor III 1803, pressure sensor IV 1804 and temperature sensor 29 are communicated to connect with controlling terminal 6, will
Collected pressure, temperature data are transmitted to controlling terminal 6 and are handled；Pressure sensor I 1801, pressure sensor II
1802, the maximum pressure that pressure sensor III 1803 and pressure sensor IV 1804 can be measured is 25MPa, and precision is
0.1%, the quantity of temperature sensor 29 is three, and three temperature sensors 29 are arranged on the side wall of visual test cabin 28,
Temperature sensor 29 is used to measure the temperature in natural gas hydrate deposits object shattering process inside visual test cabin 28, surveys
Warm range is -20 DEG C~100 DEG C.
The metering system includes drier 23, three phase separator 24 and minimum gas metering device 26, the three-phase separate
It is connected to from device 24 with gas-guide tube, the top outlet side of three phase separator 24 is connected to minimum gas metering device 26, and in three-phase
Drier 23 is provided between separator 24 and minimum gas metering device 26, through mixture derived from gas-guide tube through three phase separation
Device 24 separates gas, liquid, solid, and gas is discharged at the top of three phase separator 24, and place is dried by drier 23
Reason finally arrives minimum gas metering device 26, and minimum gas metering device 26 is for collecting water jet rock breaking gas hydrates
The gas flow generated during deposit, to collect and meter gaseous.
The simulation system includes insulating box 25, visual test cabin 28, turning supporting seat 45 and video camera 47, the overturning branch
The inner top of insulating box 25 is arranged in seat 45；The visual test cabin 28 is mounted in turning supporting seat 45, and visual test cabin 28 wraps
Visual test cabin warehouse, drive end bearing bracket 46 and rear end cap 36 are included, the drive end bearing bracket 46 is fastened on visual test cabin by sealing valve 44
The front end of warehouse, and visual window 43 is provided on drive end bearing bracket 46；The rear end cap 36 is fastened on visual examination by sealing valve 44
The rear end of testing position warehouse；Temperature is constant when insulating box 25 is used to that gas hydrates to be kept to synthesize；Visual test cabin 28 is held
It is 0~50MPa by pressure limit, outer dimension is 3000mm × 3000mm × 400mm, synthetic natural gas hydrate sediment sample
Product are having a size of 100mm × 100mm × 150mm；Visual window 43 is sapphire visual window, and sapphire visual window intensity is big, to see
It examines the shattering process of natural gas hydrate deposits object and broken moment is shot by the video camera 47 that face visual window 43 is arranged；
Sealing strip 40, sealing ring 41 axis press loading chamber 35, drive end bearing bracket 46, rear end cap 36 sealing at, the purpose is to can allow its with
Outer wall sealing, prevents gas leakage；By adjusting turning supporting seat 45, facilitate the addition and taking-up of natural gas hydrate deposits object sample.
Wherein pipe valve I 401, pipe valve II 402, pipe valve III 403, pipe valve IV 404, pipe valve V 405, pipe valve
Part VI 406, pipe valve VII 407, pipe valve VIII 408, pipe valve Ⅸ 409, pipe valve Ⅹ 410, pipe valve Ⅺ 411 and pipe valve Ⅻ
Whether 412 be connected to its place pipeline；Safety valve 19 is to control total system safety.
The applied voltage test method of fluid jet in-situ retorting gas hydrates, including following step are carried out using above-mentioned apparatus
It is rapid:
Step 1: the visual test cabin 28 of cleaning before test, places drying, prepare quartz sand or silty, cleaning is dry
Only it and dries, is cleaned in the process of cleaning using deionized water；
Step 2: quartz sand or silty are uniformly mixed with salt water, mixture is obtained, spends what ion processing was crossed
Test shovel is by mixture filling ring moulding set 33, and ring moulding covers 33 pack mixtures and is fitted into visual test cabin 28, and filling finishes
The drive end bearing bracket 46 of visual test cabin 28 and visual test cabin warehouse are tightened with sealing valve 44 afterwards, is placed in insulating box 25, passes through
Constant-flux pump 13 is filled the water into axis pressure loading chamber 35, and reaches the axis pressure of sea bed gas hydrate sedimentary original position；Pass through ring pressure
Pump 27 is filled the water to the ring of visual test cabin 28 pressure hole 38, and reaches the confining pressure of simulated sea bottom natural gas hydrate deposit original position；
Adjust the position of jet nozzle 32, jet stream spray away from, select the specification of jet nozzle 32, jet diameter, adjust jet pump 20, if
Effluxvelocity needed for setting test；
It Step 3: being passed through air into insulating box 25, will entirely visual test cabin 28 cool down in air bath, and open injection
Pipe valve I 401, pipe valve II 402 and the pipe valve III 403 of system, into visual test cabin 28 with the speed of 350mL/min
It is filled with methane gas, the charge of methane gas, general inflationtime are determined according to natural gas hydrate deposits object saturation degree
About 20min~30min；By the temperature that air bath temperature setting is near freezing point, the data obtained, after about 10h, natural gas are recorded
Lanthanum chloride hydrate finishes, and obtains natural gas hydrate deposits object sample；
Step 4: jet crushing: after gas hydrates synthesis finishes, air bath temperature being dropped to 242K~271K
Hereinafter, after stabilizing the temperature, extracting remaining methane gas out at once with vacuum pump 8, and it is natural to be quickly filled with cooling salt water submerged
Gas hydrate sediment sample adjusts the pump amount of ring press pump 27 and constant-flux pump 13 and is pumped into the time, reaches sea-bottom natural gas hydration
Air bath temperature setting is the reaction temperature of test setting by the axis pressure and confining pressure full-scale condition of object sedimentary original position；Starting is penetrated
Crushing system is flowed, jet crushing test is carried out, and shoots the process of jet crushing with video camera 47, while according to temperature/pressure sensor
29 record temperature；
Step 5: gas dosing: with the progress of jet stream, mixture is discharged from the gas-guide tube of visual test cabin 28, enters
Three phase separator 24 isolates gas, passes through 23 dry gas of drying tube；Air bath temperature is improved, will be remained in visual test cabin 28
Remaining gas hydrate dissociation finishes until decomposing, and measures the total amount of methane decomposition gas；
Step 6: after the test, closing the instruments such as jet pump 20, constant-flux pump 13, ring press pump 27, taking out visual test cabin
28, it observes and records the crushing effect of object containing natural gas hydrate deposits；Natural gas hydrate deposits object sample is taken out, cleaning is visual
Test cabin 28 analyzes data.
Claims (4)
1. the pressure test device of fluid jet in-situ retorting gas hydrates, which is characterized in that the device includes: injection system
System, jet crushing system, ring pressure system, axis pressure system, back pressure system, vacuum system, simulation system, acquisition processing system and meter
Amount system；
The injected system, axis pressure system and vacuum system are connect by admission line with the air inlet of triple valve (17), simultaneously
Two gas outlets of triple valve (17) pass through gas injecting pipe (34) respectively, axis pressure pipeline (37) is connected to simulation system, and is infusing
Pressure sensor I (1801) and pipe valve I (401) are provided in feed channel (34), injected system into simulation system for infusing
Enter the methane gas for synthesis of natural gas hydrate, and is pressurized to methane gas needed for meeting synthesis of natural gas hydrate
Pressure condition, injected system include methane gas cylinder (1), pressure reducing valve (2), pipe valve II (402), pressure regulator valve I (301), booster pump
(5), air compressor machine (7), buffer container (9), gas flow control meter (11), check valve (12) and pipe valve III (403), the first
Alkane gas cylinder (1) is by the first piping connection to admission line, in being sequentially arranged pressure reducing valve (2), pipe valve on the first pipeline
II (402), pressure regulator valve I (301), gas flow control meter (11), check valve (12) and pipe valve III (403)；The booster pump
(5) inlet end is connect by the second pipeline with air compressor machine (7), and pressure regulator valve II (302) is provided on the second pipeline, is pressurized
The outlet side of pump (5) passes through respectively in third pipeline and the 4th piping connection to the first pipeline, third pipeline and the first pipeline
Junction is located between pressure reducing valve (2) and pipe valve II (402), while pipe valve IV (404) is provided on third pipeline, and the 4th
The junction of pipeline and the first pipeline is provided between pipe valve II (402) and pressure regulator valve I (301) on the 4th pipeline
Pipe valve V (405) and pipe valve VI (406)；It is provided with pressure gauge (15) on the buffer container (9), buffer container (9) is logical
The 5th pipeline and the 4th piping connection are crossed, and the junction of the 5th pipeline and the 4th pipeline is located at pipe valve V (405) and pipe valve
Between part VI (406)；
The jet crushing system is connected to by jet pipe (31) with simulation system, and jet crushing system is used to spray to simulation system
The high pressure water flow of established natural gas hydrate deposits object inside broken simulation system is penetrated, jet crushing system includes jet pump
(20), jet pipe (31), jet nozzle (32) and elevating mechanism (30), jet pump (20) is connect with jet pipe (31), and is being penetrated
Pipe valve VII (407) is provided between stream pump (20) and jet pipe (31)；Jet pipe (31) passes through the visual test of simulation system
It is extended to inside it at the top of storehouse (28), jet pipe (31) is fixed on elevating mechanism (30), the jet stream end installation of jet pipe (31)
There are jet nozzle (32)；
The ring pressure system is connected to ring pressure hole (38) being arranged on visual test cabin (28), and ring presses system to be used for the mould
Quasi- system provides the confining pressure of sea bed gas hydrate sedimentary original position；It includes ring press pump (27) and ring moulding set that ring, which presses system,
(33), ring press pump (27) is connected to by pipeline with ring moulding set (33), and pressure sensor II (1802) is provided on the pipeline
With pipe valve VIII (408)；Ring moulding set (33) setting is internal in visual test cabin (28), ring moulding set (33) and drive end bearing bracket
(46), sealing strip (40) and sealing ring (41) are provided in the gap between visual window (43)；
The axis pressure system is connected to simulation system, and axis presses system to be used to provide sea bed gas hydrate to the simulation system
The axis pressure of sedimentary original position；Axis pressure system includes constant-flux pump (13), axis pressure pipeline (37), axis pressure loading chamber (35), loading axis
(39) and pressure plare (42), the constant-flux pump (13) is by the 6th piping connection to admission line, and sets on the 6th pipeline
It is equipped with pipe valve Ⅸ (409)；The axis pressure pipeline (37) is connected to setting in internal axis pressure loading chamber (35) of rear end cap (36)；
Loading axis (39) one end setting is internal in axis pressure loading chamber (35), and the other end of loading axis (39) passes through rear end cap (36) and prolongs
It extends to and is connect inside visual test cabin warehouse with pressure plare (42)；Between the pressure plare (42) and ring moulding set (33), load
Between axis (39) and ring moulding set (33), between loading axis (39) and rear end cap (36) and axis pressure loading chamber (35) and rear end cap
(36) sealing strip (40) and sealing ring (41) are provided at the gap between；
The back pressure system includes gas-guide tube, back-pressure valve (21), backpressure pump (22) and back pressure buffer container (10), and the one of gas-guide tube
End is connected to jet pipe (31), and the other end of gas-guide tube is connected to back pressure buffer container (10), and back pressure is provided on gas-guide tube
Valve (21), pipe valve Ⅹ (410) and pressure sensor III (1803), the back pressure buffer container (10) and backpressure pump (22) are even
It is logical, and pipe valve Ⅺ (411) is provided between back pressure buffer container (10) and backpressure pump (22)；
The vacuum system includes vacuum meter (14), vacuum tank (16) and vacuum pump (8), one end of vacuum tank (16) and true
Sky pump (8) connection, the other end of vacuum tank (16) by the 7th piping connection to admission line, on the 7th pipeline successively
It is provided with pipe valve Ⅻ (412), safety valve (19) and pressure sensor IV (1804), vacuum meter (14) setting is held in vacuum
On device (16)；
The acquisition processing system includes pressure sensor I (1801), pressure sensor II (1802), pressure sensor III
(1803), pressure sensor IV (1804), temperature sensor (29) and controlling terminal (6), pressure sensor I (1801), pressure
Sensor II (1802), pressure sensor III (1803), pressure sensor IV (1804) and temperature sensor (29) with control
Terminal (6) communication connection；
The metering system includes drier (23), three phase separator (24) and minimum gas metering device (26), the three-phase
Separator (24) is connected to gas-guide tube, and the top outlet side of three phase separator (24) is connected to minimum gas metering device (26),
And drier (23) are provided between three phase separator (24) and minimum gas metering device (26)；
The simulation system includes insulating box (25), visual test cabin (28), turning supporting seat (45) and video camera (47), described to turn over
Turn support (45) setting in the inner top of insulating box (25)；The visual test cabin (28) is mounted on turning supporting seat (45), can
It include visual test cabin warehouse, drive end bearing bracket (46) and rear end cap (36) depending on test cabin (28), the drive end bearing bracket (46) passes through sealing
Valve (44) is fastened on the front end of visual test cabin warehouse, and visual window (43) are provided on drive end bearing bracket (46)；The rear end cap
(36) rear end of visual test cabin warehouse is fastened on by sealing valve (44)；The video camera (47) is placed in visual test cabin (28)
Outside, and its face visual window (43) is arranged.
2. the pressure test device of fluid jet in-situ retorting gas hydrates according to claim 1, it is characterised in that:
The jet crushing system is 20mm at a distance from visual window (43).
3. the pressure test device of fluid jet in-situ retorting gas hydrates according to claim 1, it is characterised in that:
The piston stroke of the loading axis (39) is 30mm.
4. the pressure test device of fluid jet in-situ retorting gas hydrates according to claim 1, it is characterised in that:
The quantity of the temperature sensor (29) is three, and three temperature sensors (29) are arranged at the side wall of visual test cabin (28)
On.
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| CN201920092653.5U CN209483311U (en) | 2019-01-21 | 2019-01-21 | The pressure test device of fluid jet in-situ retorting gas hydrates |
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| CN201920092653.5U CN209483311U (en) | 2019-01-21 | 2019-01-21 | The pressure test device of fluid jet in-situ retorting gas hydrates |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109538170A (en) * | 2019-01-21 | 2019-03-29 | 吉林大学 | The pressure test device and method of fluid jet in-situ retorting gas hydrates |
| CN113445966A (en) * | 2021-08-02 | 2021-09-28 | 西南石油大学 | Ocean natural gas hydrate exploitation analogue means |
| CN114994288A (en) * | 2022-06-01 | 2022-09-02 | 重庆科技学院 | Comprehensive experiment system for preventing and controlling generation of oil and gas pipeline hydrate |
-
2019
- 2019-01-21 CN CN201920092653.5U patent/CN209483311U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109538170A (en) * | 2019-01-21 | 2019-03-29 | 吉林大学 | The pressure test device and method of fluid jet in-situ retorting gas hydrates |
| CN113445966A (en) * | 2021-08-02 | 2021-09-28 | 西南石油大学 | Ocean natural gas hydrate exploitation analogue means |
| CN114994288A (en) * | 2022-06-01 | 2022-09-02 | 重庆科技学院 | Comprehensive experiment system for preventing and controlling generation of oil and gas pipeline hydrate |
| CN114994288B (en) * | 2022-06-01 | 2023-12-12 | 重庆科技学院 | Comprehensive experiment system for preventing and controlling hydrate formation of oil and gas pipeline |
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