CN207478036U - The extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent - Google Patents
The extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent Download PDFInfo
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- CN207478036U CN207478036U CN201721744328.XU CN201721744328U CN207478036U CN 207478036 U CN207478036 U CN 207478036U CN 201721744328 U CN201721744328 U CN 201721744328U CN 207478036 U CN207478036 U CN 207478036U
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Abstract
The utility model discloses the extraction equipments of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent, including extractor, the bottom end setting discharge nozzle of extractor, discharge nozzle is connected with going out flow container, the outside of extractor is equipped with temperature controller, ultrasonic wave controller and pressure controller, go out the bottom setting outlet tube of flow container, probe tube and return duct are provided on the outlet tube, the adjustable pipe of one end sealing is arranged in outlet tube, the sealing end setting first piston of adjustable pipe, the openend setting second piston of adjustable pipe, adjustable pipe is located at first piston, between second piston, setting and first piston in outlet tube, the matched the first sliding groove of second piston；Two ends setting connecting rod of the first piston far from adjustable pipe, connecting rod stretches out outlet tube, slide first piston, second piston can control liquid from probe tube or recovery tube outflow outlet tube, first inlet tube is set on extractor, reflux pipe is set on outlet tube, reflux pipe is connected with the first inlet tube, and pump is set on reflux pipe.
Description
Technical field
The utility model is related to the extraction equipments of industrial chemicals, particularly relate to a kind of superhigh temperature ultralow permeable reservoir micro emulsion lyolysis
The extraction equipment of blocking agent.
Background technology
Microemulsion has many unique properties as separating medium, such as the spherical shape or bicontinuous structure of nanoscale, soon
The dynamical structure and property of solubilizing that speed polymerization detaches again again, while micro emulsion particle is small, thus with larger mass transfer surface
Product, can improve mass-transfer efficiency, can be applied to hydrometallurgy, geological prospecting, oil, chemical industry, environmental protection, medicine and other fields,
The content for extracting the extracting substance in stoste during extraction after single-stage extraction is higher toward contact, this just needs to carry out multistage extraction extraction
It taking, needs to connect multiple extractors, feed liquid and raffinate at different levels are all in contact with fresh extractant, and extraction yield is higher, but
Equipment causes production cost larger using more, and different extractants, extraction stoste cooperation reach extraction standard, need
Extractor quantity differ, to ensure that equipment can be applicable under various extraction conditions, the extractor of preparation can compare more, position
The number that extractor in end uses is far smaller than the access times of front end extractor, forms waste.
In addition, extraction refers to using target substance solubility or distribution coefficient in the solvent of two kinds immiscible (or slightly soluble)
Difference, a kind of method that target substance is made to be transferred to from solvent in another solvent, be purification and separation compound
Important means.By repeated multiple times extraction, the target substance of the overwhelming majority can be extracted.Since extracting operation is simple,
Without phase-change, it consumes energy low, at low cost, meanwhile, the property of target substance is not destroyed in extraction process, therefore often as target substance
One of prefered method isolated and purified.
Extraction efficiency is to weigh one important index of extraction process.In general, extraction efficiency is by acid-base value, temperature and pressure
The influence of the factors such as strong.For being extracted especially for biomaterial, the extraction conditions needed for the biomaterial of different characteristics is not
Together, therefore the biomaterial of different characteristics can improve extraction efficiency using suitable extraction mode.Life containing wood substance component
Object material needs to extract at high temperature, it is therefore desirable to improve extraction efficiency using the extraction equipment with heating function；Containing more
The biomaterial of phenol ingredient or thermally sensitive composition needs to extract at low temperature, it is therefore desirable to be filled using the extraction with refrigerating function
Put raising extraction efficiency；There are some biomaterials needs to be extracted under high pressure or low pressure, it is therefore desirable to using with being pressurized or subtract
The extraction equipment of function is pressed to improve extraction efficiency.In addition, the multistage effect generated in extraction process using ultrasonic wave, it is possible to increase object
Matter molecular motion frequency and speed increase the contact area of target component and extractant, so as to which target component be accelerated to enter extraction
Agent improves extraction efficiency.
Existing extraction equipment is often suitable only for the extraction of the biomaterial of certain specific feature, due to the life of different characteristics
The extraction conditions of object material is different, therefore need to be extracted using different extraction equipments to be directed to the biomaterial of different characteristics
It takes, this causes the applicability of existing extraction equipment limited.
Utility model content
It is a primary object of the present invention to provide a kind of microemulsion extraction equipment, liquid separation behaviour is carried out after being extracted by extractor
Make, then sample, the content of extracting substance in stoste is extracted after detection extraction, recycled and extracted by recovery tube if standard is reached
Stoste enters extractor if standard is not reached by return duct, adds in fresh extractant and is extracted, until reaching extraction
Standard is taken, multitple extraction can be completed, the waste of equipment will not be caused.
To achieve the above object, the technical solution of the utility model is a kind of superhigh temperature ultralow permeable reservoir micro emulsion lyolysis of design
The extraction equipment of blocking agent, the extraction equipment include extractor, and the bottom end setting discharge nozzle of extractor, discharge nozzle is with going out flow container company
Logical, the outside of extractor is equipped with temperature controller, ultrasonic wave controller and pressure controller, and liquid is provided in the bottom for going out flow container
It manages, probe tube and return duct is provided on the outlet tube, the adjustable pipe of one end sealing, the activity are arranged in the outlet tube
The sealing end setting first piston of pipe, the openend setting second piston of adjustable pipe, the adjustable pipe are located at first piston, second
Between piston, setting and first piston, the matched the first sliding groove of second piston in outlet tube；First piston is far from adjustable pipe
Two ends set connecting rod, and connecting rod stretches out outlet tube, slide first piston, second piston can control liquid from probe tube or return
Closed tube flows out outlet tube, and the first inlet tube is set on the extractor, reflux pipe, the reflux pipe and first are set on outlet tube
Inlet tube connects, and pump is set on reflux pipe.
Wherein preferred technical solution is one end setting third piston of the second piston far from second piston, described
The diameter of third piston is more than the diameter of second piston, is set and the matched second sliding slot of third piston in the adjustable pipe.
Preferred technical solution is in addition, set the second inlet tube, in first inlet tube and second on the extractor
The first solenoid valve and second solenoid valve are respectively equipped on inlet tube, is distinguished in the end of first inlet tube and the second inlet tube
Equipped with the first atomizer and the second atomizer.
Further preferred technical solution in the extractor in addition, being additionally provided with stirring rod, supporting rod, fixed link, floating
Ball, the first placement pole, the second placement pole, the first wind turbine, the second wind turbine, stirring rod top heavily fortified point are directly fixed in extractor inner top
At the heart, one first through hole of the hard straight setting in supporting rod middle, stirring rod passes through first through hole, and supporting rod is moved down along stirring rod
It is dynamic, it is provided with fixed link straight down at the both ends of the supporting rod, clever one end of fixed link is equipped with floating ball.
The advantages of the utility model and advantageous effect are：
1st, liquid separation operation is carried out after the utility model is extracted by extractor, is then sampled, is extracted in detection extraction stoste
The content of substance, by the extraction stoste after recovery tube recycling extraction if reach standard, if do not reach standard pass through it is anti-
Flow tube enters extractor, adds in fresh extractant and is extracted, until reaching extraction standard, it is only necessary to an extractor
Multitple extraction is completed, the waste of equipment will not be caused.
2nd, setting and the matched second sliding slot of third piston in the utility model adjustable pipe, when third piston slides into the
During the right end of two sliding slots, first piston by probe tube, recovery tube close, to the left slide motion bar first piston be located at probe tube,
Probe tube is opened between recovery tube, is opened recovery tube when third piston slides into the left end of second sliding slot, at this time second
Piston closes probe tube.
3rd, the second inlet tube is set on the utility model extractor, facilitates and extractant is added into extractor.
4th, set in agitating device extraction process and be stirred in the utility model extractor, make extractant with extraction stoste into
Row comes into full contact with, and carries extraction efficiency.
5th, the piston rod of the utility model oil cylinder and connecting rod slip adjustable pipe easy to connect, control probe tube, recovery tube
Opening and closing.
6th, since the second wind turbine, the second wind turbine are dried to mixed liquor liquid level, the atomized liquid of ullage is quickly sucked,
Then it is blown into mixed liquor, so as to accelerate the falling speed of atomized liquid:Since the first wind turbine, the second wind turbine are clockwise simultaneously
Or tilt the atomized liquid dried and entered with pressure-vaccum to mixed liquor liquid level counterclockwise simultaneously, the stirring of mixed liquor is further promoted,
Mixed liquor is made integrally to dry clockwise or counterclockwise with the second wind turbine, the second wind turbine simultaneously, liquid is promoted and integrally stirs
It mixes.Extraction speed of production and the extraction quality of production can be improved in this way.
Description of the drawings
Fig. 1 is the structure diagram of the utility model extraction equipment；
Fig. 2 is the structure diagram that first piston is located at the first sliding groove left end in the utility model extraction equipment；
Fig. 3 is the structure diagram that first piston is located at the first sliding groove right end in the utility model extraction equipment；
Fig. 4 is the structure diagram of extractor in the utility model extraction equipment.
In figure：1st, extractor；2nd, go out flow container；3rd, temperature controller；4th, outlet tube；4.1st, oil cylinder；5th, probe tube；6th, it flows back
Pipe；7th, adjustable pipe；7.1st, first piston；7.2nd, second piston；7.3rd, connecting rod；7.4th, third piston；7.5th, the first sliding groove；
7.6th, second sliding slot；8th, reflux pipe；8.1st, it pumps；9th, stirring rod；10th, first through hole；11st, discharge nozzle；12nd, the first inlet tube；13、
Second inlet tube；14th, ultrasonic wave controller；15th, pressure controller；16th, the first solenoid valve；17th, second solenoid valve；18th, first
Atomizer；19th, the second atomizer；20th, supporting rod；21st, fixed link；22nd, floating ball；23rd, the first placement pole；24th, the second placement pole；
25th, the first wind turbine；26th, the second wind turbine.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is further described.Implement below
Example is only used for clearly illustrating the technical solution of the utility model, and the protection model of the utility model cannot be limited with this
It encloses.
As shown in figures 1-4, a kind of extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent of the utility model, institute
It states extraction equipment and includes extractor 1, the bottom end setting discharge nozzle 11 of extractor 1, discharge nozzle 11 is connected with going out flow container 2, extractor 1
Outside be equipped with temperature controller 3, ultrasonic wave controller 14 and pressure controller 15, go out flow container 2 bottom setting outlet tube 4,
Probe tube 5 and return duct 6 are provided on the outlet tube 4, the adjustable pipe 7 of one end sealing, the work are arranged in the outlet tube 4
The sealing end setting first piston 7.1 of dynamic pipe 7, the openend setting second piston 7.2 of adjustable pipe 7, the adjustable pipe 7 are located at the
Between one piston 7.1, second piston 7.2, setting and first piston 7.1, second piston 7.2 matched first in outlet tube 4
Sliding slot 7.5；Two ends setting connecting rod 7.3 of the first piston 7.1 far from adjustable pipe 7, connecting rod 7.3 stretch out outlet tube 4, slide the
One piston 7.1, second piston 7.2 can control liquid from probe tube 5 or the outflow outlet tube 4 of recovery tube 6, the extractor 1
First inlet tube 12 is set, reflux pipe 8 is set on outlet tube 4, the reflux pipe 8 is connected with the first inlet tube 12, on reflux pipe 8
Setting pump 8.1.
The utility model preferred embodiment is, one end setting of the second piston 7.2 far from second piston 7.1 the
Three pistons 7.4, the diameter of the third piston 7.4 are more than the diameter of second piston 7.2, the interior setting of the adjustable pipe 7 and third
7.4 matched second sliding slot 7.6 of piston.
The utility model preferred embodiment is in addition, set the second inlet tube 13, described first on the extractor 1
The first solenoid valve 16 and second solenoid valve 17 are respectively equipped on 12 and second inlet tube 13 of inlet tube, in first inlet tube 12
The first atomizer 18 and the second atomizer 19 are respectively equipped with the end of the second inlet tube 13.
The utility model further preferred embodiment in the extractor 1 in addition, be additionally provided with stirring rod 9, support
Bar 20, fixed link 21, floating ball 22, the first placement pole 23, the second placement pole 24, the first wind turbine 25, the second wind turbine 26, stirring rod 9
Top heavily fortified point is directly fixed at 1 inner top center of extractor, one first through hole 10 of the hard straight setting in 20 middle of supporting rod, stirring rod 9
Across first through hole 10, supporting rod 20 is moved up and down along stirring rod 9, is provided with straight down at the both ends of the supporting rod 20 solid
Fixed pole 21, clever one end of fixed link 21 are equipped with floating ball 22.
Embodiment
A kind of extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent, including extractor 1, in the extractor 1
If agitating device, the agitating device includes bull stick 9, the shaft bar 9.The outside of the extractor 1 is controlled equipped with temperature
Device 3, ultrasonic wave controller 14 and pressure controller 15, bottom end setting discharge nozzle 11, the discharge nozzle 11 connect out flow container flow container
2, it is mixed first using microemulsion as extractant with extraction stoste peace certain proportion, liquid stratification after extraction obtains extraction phase
And raffinate phase, extraction phase is flowed into out flow container 2, raffinate phase enters other diversion cans (not regarded in figure).It is described go out flow container 2 on set
Outlet tube 4 is equipped with, probe tube 5, recovery tube 6 on the outlet tube 4 are set, the activity of one end sealing is arranged in the outlet tube 4
Pipe 7, the sealing end setting first piston 7.1 of the adjustable pipe 7, the openend setting second piston 7.2 of the adjustable pipe 7 are excellent
It selects and sealing ring is arranged outside first piston 7.1, second piston 7.2, increase leakproofness.The adjustable pipe 7 be located at first piston 7.1,
Between second piston 7.2, setting and first piston 7.1,72 matched the first sliding groove 7.5 of second piston in the outlet tube 4；
One end setting third piston 7.4 of the second piston 72 far from first piston 7.1, the diameter of the third piston 7.4 is more than
The diameter of second piston 7.2, the interior setting of the adjustable pipe 7 and 7.4 matched second sliding slot 7.6 of third piston.Described first
Two ends setting connecting rod 7.3 of the piston 7.1 far from adjustable pipe 7, the connecting rod 7.3 stretch out outlet tube 4, further include oil cylinder button,
The piston rod of the oil cylinder 4.1 is connect with connecting rod 7.3；When second piston 7.2 slides into the right end of the first sliding groove 7.5, the
One piston 7.1 closes probe tube 5, recovery tube 6, slide to the left motion bar first piston 7.1 be located at probe tube 5, recovery tube 6 it
Between probe tube 5 is opened, recovery tube 6 is opened when second piston 7.2 slides into the left end of the first sliding groove 7.5, at this time second
Piston 7.2 closes probe tube 5, slides first piston 7.1, second piston 7.2 can control liquid from probe tube 5 or recovery tube
6 outflow outlet tubes 4.Second inlet tube 12, the second inlet tube 13 on the extractor 1 are set, reflux is set on the outlet tube 4
Pipe 8, the reflux pipe 8 are connected with the first inlet tube 12, and setting pump 81 on the reflux pipe 8 is opened probe tube 5 and is sampled,
The content of extraction stoste (raffinate phase) interior extracting substance after detection extraction if reaching standard, opens the recycling extraction of recovery tube 6
Extraction stoste afterwards enters extractor 1 by return duct 8 if too high levels do not reach standard, adds in fresh extractant
It is extracted, until reaching extraction standard, it is only necessary to which multitple extraction can be completed in an extractor 1, will not cause the wave of equipment
Take.First inlet tube 12, goes out on the inlet tube of flow container 2 to be respectively equipped with the first solenoid valve 16 and the second electromagnetism at second inlet tube 13
Valve 17.When third piston 7.4 slides into the right end of second sliding slot 7.5, first piston 7.1 closes probe tube 5, recovery tube 6,
It slides motion bar first piston 7.1 to the left to open probe tube 5 between probe tube 5, recovery tube 6, when third piston 7.4 is slided
It moves to during the left end of second sliding slot 7.6 and opens recovery tube 6, second piston 7.2 closes probe tube 5 at this time, third piston 7.4
Probe tube 5,6 Close All of recovery tube when being moved to right end, recovery tube 6 is opened when third piston 7.4 is moved to left end, probe tube
5 close；Centre position is moved to, recovery tube 6 is closed, and probe tube 5 is opened, and is conducive to control first piston 7.1, second piston
7.2 stroke improves mixing effect by stirring rod 9, and extractant is made to be come into full contact with extraction stoste, puies forward extraction effect
Rate.
As shown in Figure 1, the extraction equipment in the utility model, further includes the supersonic oscillations for being set to 1 outer wall of extractor
Device 14, the temperature controller 3 for being set to 1 bottom of extractor, the pressure controller 15 set on 1 top of extractor, stretch into extractor 1
Internal pH electrodes and the display (not regarded in figure) set on extractor side；Display 7 includes and ultrasonic oscillator 14
The ultrasonic wave display module of connection, the temperature display module being connect with temperature controller 3, the pressure being connect with pressure controller 15
Display module and the pH display modules being connect with pH electrodes；Can ultrasound be generated by ultrasonic oscillator 14 in extraction process
Wave, the temperature in extractor 1 is adjusted by temperature controller 3, is adjusted the pressure in extractor 1 by pressure controller 15, is led to
Cross the pH value of solution in pH electrode detections extractor 1, at the same by display show current supersonic oscillations frequency, temperature,
Pressure and pH value；Suitable for the extraction of the material of different characteristics.
Extraction equipment as shown in Figure 4 is equipped with the first feed pipe 12, the first feed pipe 12 in 1 outer top left side of extractor
Second solenoid valve 16 is equipped with, 1 outer top right side of extractor is equipped with the second feed pipe 13, and the second feed pipe 13 is equipped with the second electricity
Magnet valve 17.First solenoid valve 16, second solenoid valve 17 can make corresponding first feed pipe 12, the second feed pipe 13 open and close
It closes.
First feed pipe 12, the second feed pipe 13 the port of export may be contained in extractor 1, in going out for the first feed pipe 12
Mouth end connects the first atomizer 18, the second atomizer 19 is connected in the port of export of the second feed pipe 13, in this way with certain speed
Two kinds of liquid respectively through the first feed pipe 12, the second feed pipe 13 enter corresponding second atomizer 18, the second atomizer 19
After nebulize liquid ejection, make two kinds of fog-like liquids in extractor 1 more contact mixing.
Stirring rod 9, supporting rod 20, fixed link 21, floating ball 22, the first placement pole 23, second are equipped on the top of extractor
Placement pole 24, the first wind turbine 25, the second wind turbine 26.
9 top of stirring rod heavily fortified point is directly fixed at 1 inner top center of extractor, the hard straight setting one first in 20 middle of supporting rod
Through-hole 10, stirring rod 9 pass through first through hole 10, and such supporting rod 20 can be moved up and down along stirring rod 9.
Two fixed links 21 are located at 9 lower section of supporting rod and heavily fortified point is directly fixed on 20 both ends of supporting rod, two fixed links, 20 bottom end respectively
It is equipped with two floating balls 22.The buoyancy of floating ball 22 can make top of the supporting rod 20 always situated in mixed liquor liquid level, supporting rod 20 away from
The distance of mixed liquor liquid level remains unchanged.
First placement pole 23, the second placement pole 24 are respectively positioned on 20 lower section of supporting rod, the first placement pole 23, the second placement pole 24
20 both ends of supporting rod are respectively and vertically fixed at, so that junction is equal away from the distance at 20 center of supporting rod, and the first placement pole
23rd, the second placement pole 24 is respectively located in two planes vertical with supporting rod 20.First placement pole 23, the second placement pole 24
It is located at respectively and both sides is faced directly by the heavily fortified point of supporting rod 20, i.e., the heavily fortified point formed positioned at supporting rod 20 and fixed link 21 faces both sides directly.The
One placement pole 23, the second placement pole 24 are acute angle with the angle faced directly by the heavily fortified point of supporting rod 20, and the first wind turbine 25 is set to
First placement pole, 23 bottom end, the air outlet of the first wind turbine 25 are located at the lower face of the first wind turbine 25, the air inlet of the first wind turbine 25
Positioned at the upper surface of the first wind turbine 25, the wind direction that the first wind turbine 25 is dried is parallel to the first placement pole 23, and the second wind turbine 26 is set
Be placed in 24 bottom end of the second placement pole, the air outlet of the second wind turbine 26 is located at the lower face of the second wind turbine 26, the second wind turbine 26 into
Air port is located at the upper surface of the second wind turbine 26, and the wind direction that the second wind turbine 26 is dried is parallel to the second placement pole 24, even if first
25 and second wind turbine 26 of wind turbine blows inclined wind on mixed liquor liquid level, since the second wind turbine 25, the second wind turbine 26 are located at respectively
The heavily fortified point that supporting rod 20 is formed with fixed link 21 faces both sides directly, makes the first wind turbine 25, the second wind turbine 26 simultaneously towards mixed liquor liquid level
It dries or dries counterclockwise towards mixed liquor liquid level simultaneously clockwise.Such second wind turbine 25, the second wind turbine 26 can be mixing
Fog-like liquid on liquid liquid level quickly after air inlet sucks, is quickly blowed in mixed liquor from air outlet, so as to accelerate extraction
The speed of production of device will not influence production because of the slow landing of fog-like liquid.In addition, due to the first wind turbine 25, the second wind turbine
26 atomized liquids entered counterclockwise to mixed liquor liquid level inclination blowing and pressure-vaccum clockwise or simultaneously simultaneously, further promote mixed
The stirring of liquid is closed, while makes mixed liquor whole and dries clockwise or counterclockwise with the second wind turbine 25, the second wind turbine 25, is promoted
It is integrally stirred into liquid.
First wind turbine 25,26 bottom position of the second wind turbine are above 22 bottom position of floating ball.Because it is necessary that floating ball 22 provides buoyancy
Some floating ball 22 is located in mixing liquid, therefore the first wind turbine 25,26 bottom position of the second wind turbine are above the floating ball 22 most
Bottom, to keep using effect.
The extraction equipment further includes controller, and temperature controller 3, ultrasonic oscillator 14, pressure are connected by controller
Controller, can be fixed on extraction by controller 15, the first solenoid valve 16, second solenoid valve 17, the first wind turbine 25, the second wind turbine 26
The outer top of tank 1.
As described above, only possible embodiments of the utility model are not used for limiting the utility model implementation
Range, i.e., all equivalent changes and modifications made according to present utility model application the scope of the claims are all the utility model patent model
It encloses and is covered.
Claims (4)
1. the extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent, which is characterized in that the extraction equipment includes extraction
Tank (1), the bottom end setting discharge nozzle (11) of extractor (1), discharge nozzle (11) are connected with going out flow container (2), the outside of extractor (1)
Equipped with temperature controller (3), ultrasonic wave controller (14) and pressure controller (15), go out the bottom setting outlet tube of flow container (2)
(4), probe tube (5) and return duct (6) are provided on the outlet tube (4), the work of one end sealing is arranged in the outlet tube (4)
Dynamic pipe (7), the sealing end setting first piston (7.1) of the adjustable pipe (7), the openend setting second piston of adjustable pipe (7)
(7.2), the adjustable pipe (7) is between first piston (7.1), second piston (7.2), setting and first in outlet tube (4)
Piston (7.1), second piston (7.2) matched the first sliding groove (7.5)；Two ends of the first piston (71) far from adjustable pipe (7)
Connecting rod (7.3) is set, connecting rod (7.3) stretches out outlet tube (4), slide first piston (7.1), second piston (7.2) can be with
Control liquid that the first inlet tube is set from probe tube (5) or recovery tube (6) outflow outlet tube (4), the extractor (1)
(12), reflux pipe (8) is set on outlet tube (4), and the reflux pipe (8) connects with the first inlet tube (12), and reflux pipe is set on (8)
Put pump (8.1).
2. the extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent as described in claim 1, the second piston
(7.2) one end setting third piston (7.4) far from second piston (7.1), the diameter of the third piston (7.4) are more than second
The diameter of piston (7.2), the interior setting of the adjustable pipe (7) and third piston (7.4) matched second sliding slot (7.6).
3. the extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent as claimed in claim 2, on the extractor (1)
Second inlet tube (13) is set, the first solenoid valve is respectively equipped on first inlet tube (12) and the second inlet tube (13)
(16) and second solenoid valve (17), the first mist is respectively equipped in the end of first inlet tube (12) and the second inlet tube (13)
Change device (18) and the second atomizer (19).
4. the extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent as claimed in claim 2, in the extractor (1)
Inside it is additionally provided with stirring rod (9), supporting rod (20), fixed link (21), floating ball (22), the first placement pole (23), the second placement pole
(24), the first wind turbine (25), the second wind turbine (26), stirring rod (9) top heavily fortified point are directly fixed at extractor (1) inner top center,
Supporting rod (20) middle one first through hole of hard straight setting (10), stirring rod (9) is across first through hole (10), supporting rod (20) edge
Stirring rod (9) moves up and down, and is provided with fixed link (21) straight down at the both ends of the supporting rod (20), fixed link (21)
Clever one end is equipped with floating ball (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721744328.XU CN207478036U (en) | 2017-12-14 | 2017-12-14 | The extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721744328.XU CN207478036U (en) | 2017-12-14 | 2017-12-14 | The extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent |
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| Publication Number | Publication Date |
|---|---|
| CN207478036U true CN207478036U (en) | 2018-06-12 |
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|---|---|---|---|
| CN201721744328.XU Active CN207478036U (en) | 2017-12-14 | 2017-12-14 | The extraction equipment of superhigh temperature ultralow permeable reservoir microemulsion plugging removal agent |
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| Country | Link |
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| CN (1) | CN207478036U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109529408A (en) * | 2019-01-18 | 2019-03-29 | 北京兴通泰克科技发展有限公司 | A kind of superhigh temperature ultralow permeable reservoir microemulsion plugging removal technology |
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2017
- 2017-12-14 CN CN201721744328.XU patent/CN207478036U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109529408A (en) * | 2019-01-18 | 2019-03-29 | 北京兴通泰克科技发展有限公司 | A kind of superhigh temperature ultralow permeable reservoir microemulsion plugging removal technology |
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