CN207904186U - Mobile oil-sand in-situ treatment device - Google Patents
Mobile oil-sand in-situ treatment device Download PDFInfo
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- CN207904186U CN207904186U CN201721726789.4U CN201721726789U CN207904186U CN 207904186 U CN207904186 U CN 207904186U CN 201721726789 U CN201721726789 U CN 201721726789U CN 207904186 U CN207904186 U CN 207904186U
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Abstract
The utility model is related to a kind of mobile oil-sand in-situ treatment devices, including：Natural gas refining separator, charging gear, drawing mechanism and pyrolysis installation；The pyrolysis installation is equipped with feed inlet, slag notch and pyrolysis gas outlet, the feed inlet are connected with charging gear, and the pyrolysis gas outlet is connected with natural gas refining separator, the slag notch is connected with drawing mechanism, which is used for that greasy dirt sand heat resolve will be contained；The charging gear is used for receiving sand containing greasy dirt and being transported in pyrolysis installation；The drawing mechanism is used for being discharged after cooling down to high temperature furnace slag；The natural gas refining separator is used for carrying out separating-purifying to the pyrolysis gas that pyrolysis gas outlet is discharged, and obtains natural gas to be recycled.The mobile oil-sand in-situ treatment device of the utility model allows oil-sand environmental protection processing in situ, greatly improves treatment effeciency.
Description
Technical field
The utility model is related to a kind of in-situ treatment device, more particularly to a kind of mobile oil-sand in-situ treatment device.
Background technology
Oil-sand refers to the settling sand rich in bitumen.Therefore also referred to as " tar sand ".Oil-sand be substantially a kind of pitch,
Husky, rich ore clay and water mixture, wherein bitumen content is 10~12%, and the mineral such as husky and clay account for 80~85%, remainder
For 3~5% water.Have the characteristics that high density, high viscosity, high C/Hratio and high metal content.
China is abundant one of the country of world's oil-sand ore resources, occupies the 5th, the world.The general supposition of expert, in conjunction with first
Step investigation result thinks that Chinese oil-sand resource potentiality are likely larger than viscous crude resource, and preresearch estimates China oil-sand has hundred billion tons, can adopt
10,000,000,000 tons or so of petroleum resource cities.Main problem existing for existing oil-sand processing method is that processing equipment is bulky, place
Manage inefficiency.
Utility model content
The technical issues of the utility model will solve in the prior art provides a kind of mobile oil-sand in-situ treatment device.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is specific as follows：
A kind of movable type oil-sand in-situ treatment device, including：Natural gas refining separator, charging gear, drawing mechanism,
And pyrolysis installation；
The pyrolysis installation is equipped with feed inlet, slag notch and pyrolysis gas outlet, and the feed inlet is connected with charging gear,
The pyrolysis gas outlet is connected with natural gas refining separator, and the slag notch is connected with drawing mechanism, which uses
By oil-sand heat resolve；
The charging gear is used for receiving oil-sand and being transported in pyrolysis installation；
The drawing mechanism is used for being discharged after cooling down to high temperature furnace slag；
The natural gas refining separator is used for carrying out separating-purifying to the pyrolysis gas that pyrolysis gas outlet is discharged, and obtains
Natural gas is to be recycled；
The natural gas refining separator includes：Knockout drum ontology, top are equipped with gas outlet, natural for being discharged
Gas；Bottom end is equipped with oil discharge outlet, for the fluid flow down is discharged；Side wall is equipped with air inlet, for being passed through pending mixing
Gas；
The outer layer of knockout drum ontology is coated by coolant jacket, for being cooled down to internal gaseous mixture；
The intrinsic top of knockout drum is equipped at least one nozzle tip, for spraying fluid；In the lower section of nozzle tip, air inlet
The position of mouth top is equipped at least one layer of sintered plate for carrying multiple oil leaking holes, for accepting the fluid that nozzle tip sprays, and will
Fluid is leaked down by oil leaking hole, realizes the cleaning to the gaseous mixture ramped up by oil leaking hole.
In the above-mentioned technical solutions, the temperature of the coolant liquid flowed in the coolant jacket is 100-180 DEG C.
In the above-mentioned technical solutions, the charging gear includes successively from top to bottom：
Material bearing disc, for accepting pending oil-sand；
Second feed pipe, the upper end are connected with material bearing disc lower end；
First feed pipe is horizontally disposed with, and right end is connected with pyrolysis installation, top center position and second feed pipe
Lower end be connected；
The second stick pusher is equipped in the material bearing disc, which can up and down reciprocatingly be transported by the effect of the second push rod
It is dynamic, by oil-sand by pushing to the bottom of the second feed pipe in the material bearing disc；
Left end in first feed pipe is equipped with the first stick pusher, which can be acted on by the first push rod
Bilateral reciprocation will be pushed to by the oil-sand in the second feed pipe bottom dropped out to first feed pipe in pyrolysis installation.
In the above-mentioned technical solutions, the length of first stick pusher is more than the diameter of second feed pipe.
In the above-mentioned technical solutions, the drawing mechanism includes：
First transfer canal is arranged at the slag notch of pyrolysis installation, and one end is connected with the slag notch, and the other end connects
It is connected to connecting pipe；
Second transfer canal is arranged below first transfer canal, and one end is connect with the connecting pipe, another
End is equipped with discharge port；
The outer layer of first transfer canal and second transfer canal is respectively equipped with water-cooled jacket；
The first screw conveyor is equipped in first transfer canal, the dregs that can fall slag notch is delivered to described
At connecting pipe, fall in second transfer canal；
It is equipped with the second screw conveyor in second transfer canal, the dregs that the connecting pipe is fallen can be conveyed
It is discharged to discharge port.
In the above-mentioned technical solutions, the length of first transfer canal and second transfer canal is respectively 0.5~5
Rice, diameter is respectively 0.2~2 meter.
In the above-mentioned technical solutions, the pyrolysis installation includes：
Heating mantle, left end be equipped with feed inlet, right end be equipped with slag notch and pyrolysis gas outlet, the pyrolysis gas outlet be used for
Natural gas refining separator is connected；
Heated mandrel, is arranged the center in the heating mantle, and both ends are connected by the first connection section and second respectively
Logical section is connected to the both ends of the heating mantle；
The first connection section is connected with air inlet, and the second connection section is connected with gas outlet；High-temperature fuel gas can be from institute
It states air inlet to be passed through, being circulated to the gas outlet by heating mantle and heated mandrel is discharged.
In the above-mentioned technical solutions, the heating mantle inner wall is equipped with multiple outer pushing sheets, can be with the heating mantle
Rotation, push oil-sand move from left to right；And/or the heated mandrel outer wall is equipped with multiple interior pushing sheets, it can be with institute
The rotation of heated mandrel is stated, oil-sand is pushed to move from left to right.
In the above-mentioned technical solutions, the top of the outer pushing sheet is equipped with " L " shape structure；And/or the interior pushing sheet
Top be equipped with " L " shape structure.
The utility model has advantageous effect below：
The mobile oil-sand in-situ treatment device of the utility model allows oil-sand environmental protection processing in situ, greatly carries
High treatment effeciency.
Natural gas refining separator in the utility model carries out Oil-gas Separation, by device using cyclone
Fluid spray equipment and the sintered plate with oil leaking hole is arranged in top, and efficiently separating for natural gas is realized by gas-liquid convection, to
The volume for effectively reducing natural gas refining separator, greatly strengthens operability, realizes mobile natural gas purification
Separation.
The content for the natural gas that natural gas refining separator in the prior art purifies out is 90% hereinafter, and this reality
The content of natural gas can be increased to 98% or more with the natural gas refining separator in novel.
Natural gas refining separator in the utility model, purification efficiency is high, small, can be placed in truck and move up
It is dynamic to use.
Charging gear in the utility model is arranged by unique mechanical structure, realizes oil-sand is continual defeated
It send to oil-sand processing equipment.Charging gear in the utility model is suitable for handling viscous poor fluidity, viscosity is high, and dosage is big
Oil-sand.
Drawing mechanism in the utility model is set at the slag notch of oil/sand separator pyrolysis installation, passes through two
The transfer canal setting of grade, limits the refluence of air, effectively prevents the generation of deflagration accident well.
Drawing mechanism in the utility model, volume compact are suitble to the row with the pyrolysis installation mounted on packaged type
At cinder notch, play the role of safe deslagging.
Pyrolysis installation in the utility model is integrally carried out while being heated to pyrolysis installation by high-temperature fuel gas, realized
The high-efficiency thermal decomposition of oil-sand greatly reduces the volume and weight of pyrolysis installation so that it can be placed in mobile working on truck.
Pyrolysis installation in the utility model is respectively equipped with labyrinth catch in heating mantle and heated mandrel, plays and delay height
Warm combustion gas further improves the efficiency of heating surface by the effect of speed.
Pyrolysis installation in the utility model, by the way that outer pushing sheet and interior pusher are respectively set in heating mantle and heated mandrel
Piece so that oil-sand can obtain heat, fast pyrogenation respectively from heating mantle and heated mandrel.
Description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
Fig. 1 is a kind of structural representation of specific implementation mode of the mobile oil-sand in-situ treatment device of the utility model
Figure.
Fig. 2 is a kind of structural schematic diagram of specific implementation mode of the natural gas refining separator in the utility model.
Fig. 3 is the structural schematic diagram of the oil-sand separation charging gear in the utility model.
Fig. 4 is a kind of structural schematic diagram of working condition of oil-sand separation charging gear in the utility model.
Fig. 5 is the structural schematic diagram of oil-sand separation charging gear another working condition in the utility model.
Fig. 6 is the structural schematic diagram of the oil-sand separation drawing mechanism and oil-sand separation pyrolysis installation of the utility model.
Fig. 7 is the A-A schematic cross-sectional views in oil-sand separation pyrolysis installation shown in fig. 6.
Reference numeral in figure is expressed as：
1- natural gas refining separators；2- charging gears；3- drawing mechanisms；4- pyrolysis installations；
The first air inlets of 101-；102- oil discharge outlets；103- oil leaking holes；104- sintered plates；105- nozzle tips；106- first goes out
Gas port；107- coolant jackets；108- knockout drum ontologies.
The first stick pushers of 201-；The second stick pushers of 202-；203- material bearing discs；The first push rod of 204-；205- second is pushed
Bar；The first feed pipes of 206-；The second feed pipes of 207-.
The first transfer canals of 301-；The second transfer canals of 302-；303- slag notches；304- discharge ports；The second spirals of 305-
Conveyer；306- water-cooled jackets；307- connecting pipes；The first screw conveyors of 311-.
401- heating mantles；The outer pushing sheets of 402-；Pushing sheet in 403-；404- heated mandrels；The labyrinths 405- catch；406- second
Air inlet；The second gas outlets 407-；The connection sections of 408- first；The connection sections of 409- second.
Specific implementation mode
The utility model is described in detail below in conjunction with the accompanying drawings.
As shown in Figure 1, the mobile oil-sand in-situ treatment device of the utility model, including：Natural gas refining separator
1, charging gear 2, drawing mechanism 3 and pyrolysis installation 4；The charging gear 2 is used for receiving oil-sand and being transported to pyrolysis
In device 4；The feed inlet of the pyrolysis installation 4 is connected with charging gear 2, pyrolysis gas outlet and natural gas refining separator 1
The first air inlet 101 be connected, slag notch 303 is connected with drawing mechanism 3, and the pyrolysis installation 4 is for by oil-sand heat resolve；Institute
Drawing mechanism 3 is stated to be used for carrying out cooling discharge to high temperature furnace slag；The natural gas refining separator 1 is used for pyrolysis gas outlet
Pyrolysis gas is discharged and carries out separating-purifying, obtains natural gas to be recycled.
With reference to Fig. 1~7 respectively to the natural gas refining in the mobile oil-sand in-situ treatment device of the utility model
Separator 1, charging gear 2, drawing mechanism 3 and pyrolysis installation 4 are described in detail.
1- natural gas refining separators
Natural gas refining separator in the utility model carries out Oil-gas Separation, by filling using cyclone
Fluid spray equipment and the sintered plate with oil leaking hole is arranged in top set end, and efficiently separating for natural gas is realized by gas-liquid convection.It should
Natural gas refining separator effectively reduces the volume of natural gas refining separator, greatly strengthens operability, realizes
Mobile natural gas purification ＆ isolation.
Fig. 2 shows a kind of specific implementation mode of the natural gas refining separator 1 in the utility model.Natural air lift
Pure separator 1 includes a knockout drum ontology 108, and top is equipped with the first gas outlet 106, for natural gas is discharged；Bottom end
Equipped with oil discharge outlet 102, for the fluid flow down is discharged；Side wall is equipped with the first air inlet 101, for being passed through pending mix
Close gas.The outer layer of knockout drum ontology 108 is coated by coolant jacket 107, for being cooled down to internal gaseous mixture.Described first into
The structure of gas port 101 is venturi tube structure, is monitored with the flow to gaseous mixture.Meanwhile first air inlet 101 be connected with
Power plant is used for gaseous mixture high speed spraying into knockout drum ontology 108.The temperature of the coolant liquid flowed in the coolant jacket 107
Degree is 120 DEG C.
Natural gas refining separator 1 in the utility model, the top in knockout drum ontology 108 are equipped with 2 oil spouts
First 105, it is used for spraying fluid to entire sintered plate 104；In the lower section of two nozzle tips 105, the position of 101 top of the first air inlet
Install one layer carry multiple oil leaking holes 103 sintered plate 104, for accept nozzle tip 105 ejection fluid, and by fluid by
Oil leaking hole 103 leaks down.
Natural gas refining separator 1 in the utility model during the work time, is entered by 101 high speed of the first air inlet
Oil, water, dirt, natural gas mixture inside knockout drum ontology 108 carry out cyclonic separation in the space of 104 lower part of sintered plate.
Under the cooling effect of coolant jacket 107, most of oil, water, dirt falls downward, the natural gas gaseous mixture with oil, water ramp up,
After by the sintered plate 104 with oil leaking hole 103, it is discharged and is collected by first gas outlet 106 on top.
In this course, the fluid to be leaked down by oil leaking hole 103 is realized to the gaseous mixture that is ramped up by oil leaking hole 103
Cleaning.Specifically, the fluid part in gaseous mixture is absorbed and filter out by the fluid to leak down；It is purer after filtering
Natural gas is discharged and is collected by first gas outlet 106 on 108 top of knockout drum ontology；Fluid part is by 108 bottom of knockout drum ontology
The oil discharge outlet 102 at end is discharged, and is conducted to nozzle tip 105 again and is recycled.
In other specific implementation modes, the quantity of nozzle tip can also be reduced to 1, either increase as 3 or
More, as long as the flow of spray fluid meets the cleaning to the gaseous mixture ramped up by oil leaking hole, which is not described herein again.
2- charging gears
As seen in figures 3-5, the charging gear 2 in the utility model its include successively from top to bottom：Material bearing disc 203, second
Feed pipe 207 and the first feed pipe 206.Wherein, material bearing disc 203 is used for accepting pending oil-sand；Second feed pipe 207
Upper end is connected with 203 lower end of material bearing disc, for material bearing disc 203 and the first feed pipe 206 is connected；First feed pipe, 206 level is set
It sets, right end is connected with pyrolysis installation 4, and top center position is connected with the lower end of second feed pipe 207.
The second stick pusher 202 is equipped in the material bearing disc 203, which can be by the work of the second push rod 205
With pumping, by oil-sand by pushing to the bottom of the second feed pipe 207 in the material bearing disc 203；Second feeding
A diameter of 150mm of pipe 207.
Left end in first feed pipe 206 is equipped with the first stick pusher 201, which can be pushed away by first
The effect bilateral reciprocation for sending bar 204, will be by the oil in 207 bottom dropped out of the second feed pipe to first feed pipe 206
Sand pushes in pyrolysis installation 4.The length of first stick pusher 201 is 180mm.
Charging gear 2 in the utility model fills pending oil-sand to material bearing disc 203 first during the work time；
Start the first push rod 204 and the work of the second push rod 205, drives the first stick pusher 201 and the action of the second stick pusher 202.Such as
Shown in Figure 4 and 5, when 202 stroke of the second stick pusher to the second 207 bottom of feed pipe, the right end stroke of the first stick pusher 201 to
The left side of two feed pipes 207；The right end stroke of first stick pusher 201 to the second feed pipe 207 right side when, the second stick pusher
202 stroke highest points.First stick pusher 201 is identical with the stroke cycle of the second stick pusher 202.On a left side for the first stick pusher 201
Under the collective effect of right reciprocating action and the second stick pusher 202 up and down reciprocatingly acted, oil-sand is just transported to the first feeding
In the connected pyrolysis installation 4 of 206 right end of pipe.
3- drawing mechanisms
As shown in fig. 6, the drawing mechanism 3 in the utility model, the pyrolysis installation 4 being arranged in oil/sand separator goes out
At cinder notch 303.The pending original oil-sand come in from feed inlet can be delivered to slag notch 303 by the pyrolysis installation 4, and conveyed
In the process, using high temperature by original oil-sand carry out resolution process, behind be discussed in greater detail.Go out the dregs of discharge in slag notch 303
Temperature is generally at 600 DEG C or so.
Drawing mechanism 3 in the utility model includes upper and lower first transfer canal, 301 and second dispatch tube disposed in parallel
Road 302.Wherein, one end of the first transfer canal 301 is connected with the slag notch 303, and the other end is connected with connecting pipe 307；
Second transfer canal 302 is arranged below the first transfer canal 301, and one end is connect with connecting pipe 307, and the other end is equipped with out
Material mouth 304.The length of first transfer canal 301 and the second transfer canal 302 is respectively 2 meters, and diameter is respectively 0.3 meter.
The outer layer of first transfer canal 301 and second transfer canal 302 is respectively equipped with water-cooled jacket 306, the water
Cold set 306 is used for cooling down the high temperature dregs in first transfer canal 301 and second transfer canal 302.Water-cooled jacket 306
Interior water temperature is at 5~50 DEG C or so.
The first screw conveyor 311, the dregs that slag notch 303 can be fallen are equipped in first transfer canal 301
It is delivered at the connecting pipe 307, falls in second transfer canal 302；It is equipped in second transfer canal 302
The dregs that the connecting pipe 307 is fallen can be delivered to discharge port 304 and is discharged by the second screw conveyor 305.From discharge port
The temperature of the dregs of 304 discharges is generally at 100-180 DEG C or so.
During the work time, the dregs fallen by slag notch 303 is by for oil-sand separation drawing mechanism 3 in the utility model
One screw conveyor 311 is delivered at connecting pipe 307, is fallen in second transfer canal 302, later again by the second spiral shell
Rotation conveyer 5 is delivered to the discharge of discharge port 304.In this course, dregs is cooled to 120 DEG C or so by 600 DEG C or so.The
Air pressure in one transfer canal 301 and the second transfer canal 302 remains micro-positive pressure, i.e., less times greater than outside discharge port 304
Atmospheric pressure, play the role of preventing air from pouring in down a chimney entrance well, effectively prevent deflagration accident.
In other specific implementation modes, the length of the first transfer canal and the second transfer canal may be 0.5~5
Other numerical value in rice range, diameter may be other numerical value within the scope of 0.2~2 meter, and concrete numerical value can be according to oil-sand
The treating capacity of separator is arranged on demand under the premise of ensuring against air and pouring in down a chimney with smooth deslagging, and which is not described herein again.
4- pyrolysis installations
Pyrolysis installation in the utility model realizes oil by improving the heat exchanger effectiveness of oil-sand and pyrolysis installation
The high-efficiency thermal decomposition of sand greatly reduces the volume and weight of pyrolysis installation.
As shown in Figures 6 and 7, the pyrolysis installation 4 in the utility model includes：Heating mantle 401 and heated mandrel 404.Heating mantle
401 left end is equipped with feed inlet, and right end is equipped with slag notch 303, is respectively intended to add pending oil-sand raw material and is connected to discharging dress
3 are set so that the oil-sand after cooling treatment is discharged.The right end of heating mantle 401 is additionally provided with pyrolysis gas outlet, is used for and natural gas refining point
The first air inlet 101 from device 1 is connected.Feed inlet and pyrolysis gas outlet are not shown in FIG. 6.Heated mandrel 404 is arranged
Center in the heating mantle 401, both ends are connected to section 408 by first respectively and the second connection section 409 adds with described
The both ends of hot jacket 401 are connected to.As shown in fig. 6,401 inner wall of heating mantle is equipped with multiple outer pushing sheets 402,404 outer wall of heated mandrel
Multiple interior pushing sheets 403 are equipped with, outer pushing sheet 402 and interior pushing sheet 403 can push oil with the rotation of heating mantle 401
Sand moves from left to right.
First connection section 408 is connected with the second air inlet 406, and the second connection section 409 is connected with the second gas outlet 407；It is high
Warm combustion gas can be passed through from second air inlet 406, and second gas outlet is circulated to by heating mantle 401 and heated mandrel 404
407 discharges.Heating mantle 401 and heated mandrel 404 are internally provided with multiple labyrinth catch 405, which can delay high temperature
Combustion gas passes through, and then plays the role of improving heat exchanger effectiveness.
During the work time, high-temperature fuel gas is passed through pyrolysis installation 4 in the utility model by second air inlet 406 on right side
In first connection section 408, the conducting Jing Guo heating mantle 401 and heated mandrel 404 respectively later is sent to the second connection section in left side
At 409, it is discharged again by the second gas outlet 407 later.High-temperature fuel gas realizes in above-mentioned conductive process to 401 He of heating mantle
The heating of heated mandrel 404, and then realize outer pushing sheet 402 to being connected in heating mantle 401 and heated mandrel 404 and interior
The heating of pushing sheet 403.When outer pushing sheet 402 and interior pushing sheet 403 push oil-sand to move from left to right, just oil-sand is carried out
Sufficient heating.As shown in fig. 7, outer pushing sheet 402 and interior pushing sheet 403 are equipped with L-shaped structure on top, oil-sand is being pushed
During advance, plays the role of stirring oil-sand, more fully realize the heat exchange between oil-sand.
The inside of heating mantle 401 and heated mandrel 404 further respectively has labyrinth catch 405, which is delaying height
Warm combustion gas by while, sufficient heat exchange has been carried out with high-temperature fuel gas, so that heating mantle 401 and heated mandrel 404
The abundant heating of high-temperature fuel gas is obtained.To which the inner wall of heating mantle 401 and the outer wall of heated mandrel 404 can also be to being advanced over
Oil-sand in journey is adequately heated.
Pyrolysis installation 4 in the utility model is integrally carried out while being heated to pyrolysis installation by high-temperature fuel gas, realized
The high-efficiency thermal decomposition of oil-sand greatly reduces the volume and weight of pyrolysis installation so that it can be placed in mobile working on truck.
Obviously, the above embodiments are merely examples for clarifying the description, and does not limit the embodiments.It is right
For those of ordinary skill in the art, can also make on the basis of the above description it is other it is various forms of variation or
It changes.There is no necessity and possibility to exhaust all the enbodiments.And it is extended from this it is obvious variation or
It changes still within the protection scope of the invention.
Claims (7)
1. a kind of movable type oil-sand in-situ treatment device, which is characterized in that including：Natural gas refining separator (1), feed dress
It sets (2), drawing mechanism (3) and pyrolysis installation (4)；
The pyrolysis installation (4) is equipped with feed inlet, slag notch (303) and pyrolysis gas outlet, the feed inlet and charging gear
(2) it is connected, the pyrolysis gas outlet is connected with natural gas refining separator (1), the slag notch (303) and drawing mechanism
(3) it is connected, which is used for that greasy dirt sand heat resolve will be contained；
The charging gear (2) is used for receiving sand containing greasy dirt and be transported in pyrolysis installation (4)；
The drawing mechanism (3) is used for being discharged after cooling down to high temperature furnace slag；
The natural gas refining separator (1) is used for carrying out separating-purifying to the pyrolysis gas that pyrolysis gas outlet is discharged, and obtains
Natural gas is to be recycled；
The natural gas refining separator (1) includes：Knockout drum ontology (108), top are equipped with gas outlet (106), are used for
Natural gas is discharged；Bottom end is equipped with oil discharge outlet (102), for the fluid flow down is discharged；Side wall is equipped with air inlet (101), uses
To be passed through pending gaseous mixture；
The outer layer of knockout drum ontology (108) is coated by coolant jacket (107), for being cooled down to internal gaseous mixture；
Top in knockout drum ontology (108) is equipped at least one nozzle tip (105), for spraying fluid；In nozzle tip (105)
Lower section, the position above air inlet (101) is equipped at least one layer of sintered plate (104) for carrying multiple oil leaking holes (103), is used for
The fluid that nozzle tip (105) sprays is accepted, and fluid is leaked down by oil leaking hole (103), is realized to being ramped up by oil leaking hole (103)
Gaseous mixture cleaning；
The charging gear (2) includes successively from top to bottom：
Material bearing disc (203), for accepting pending sand containing greasy dirt；
Second feed pipe (207), the upper end are connected with material bearing disc (203) lower end；
First feed pipe (206) is horizontally disposed with, and right end is connected with oil sand processing unit, top center position and described second
The lower end of feed pipe (207) is connected；
The second stick pusher (202) is equipped in the material bearing disc (203), which can be by the second push rod (205)
Effect pump, greasy dirt sand will be contained by pushing to the bottoms of the second feed pipe (207) in the material bearing disc (203)；
Left end in first feed pipe (206) is equipped with the first stick pusher (201), which can be by first
The effect bilateral reciprocation of push rod (204), will be by the second feed pipe (207) bottom dropped out to first feed pipe
(206) sand containing greasy dirt in pushes in oil sand processing unit；
The drawing mechanism (3) includes：
First transfer canal (301) is arranged at the slag notch (303) of pyrolysis installation (4), one end and the slag notch
(303) it is connected, the other end is connected with connecting pipe (307)；
Second transfer canal (302), setting is below first transfer canal (301), one end and the connecting pipe
(307) it connects, the other end is equipped with discharge port (304)；
The outer layer of first transfer canal (301) and second transfer canal (302) is respectively equipped with water-cooled jacket (306)；
The first screw conveyor (311), the slag that slag notch (303) can be fallen are equipped in first transfer canal (301)
Soil is delivered at the connecting pipe (307), is fallen in second transfer canal (302)；
It is equipped with the second screw conveyor (305) in second transfer canal (302), the connecting pipe (307) can be fallen
The dregs fallen is delivered to discharge port (304) discharge.
2. movable type oil-sand in-situ treatment device according to claim 1, which is characterized in that in the coolant jacket (107)
The temperature of the coolant liquid flowed is 100-180 DEG C.
3. movable type oil-sand in-situ treatment device according to claim 1, which is characterized in that first stick pusher
(201) length is more than the diameter of second feed pipe (207).
4. movable type oil-sand in-situ treatment device according to claim 1, which is characterized in that first transfer canal
(301) and the length of second transfer canal (302) is respectively 0.5~5 meter, and diameter is respectively 0.2~2 meter.
5. movable type oil-sand in-situ treatment device according to claim 1, which is characterized in that pyrolysis installation (4) packet
It includes：
Heating mantle (401), left end are equipped with feed inlet, and right end is equipped with slag notch (303) and pyrolysis gas outlet, the pyrolysis gas outlet
For being connected with natural gas refining separator (1)；
Heated mandrel (404), the center being arranged in the heating mantle (401), both ends are saved by the first connection respectively
(408) it is connected to the both ends of the heating mantle (401) with the second connection section (409)；
The first connection section (408) is connected with air inlet (406), the second connection section (409) and gas outlet (407) phase
Even；High-temperature fuel gas can be passed through from the air inlet (406), and the outlet is circulated to by heating mantle (401) and heated mandrel (404)
Mouth (407) discharge.
6. movable type oil-sand in-situ treatment device according to claim 5, which is characterized in that in the heating mantle (401)
Wall is equipped with multiple outer pushing sheets (402), oil-sand can be pushed to move from left to right with the rotation of the heating mantle (401)；
And/or
Heated mandrel (404) outer wall be equipped with multiple interior pushing sheets (403), can with the rotation of the heated mandrel (404),
Oil-sand is pushed to move from left to right.
7. movable type oil-sand in-situ treatment device according to claim 6, which is characterized in that the outer pushing sheet (402)
Top be equipped with " L " shape structure；And/or
The top of the interior pushing sheet (403) is equipped with " L " shape structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721726789.4U CN207904186U (en) | 2017-12-12 | 2017-12-12 | Mobile oil-sand in-situ treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721726789.4U CN207904186U (en) | 2017-12-12 | 2017-12-12 | Mobile oil-sand in-situ treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207904186U true CN207904186U (en) | 2018-09-25 |
Family
ID=63567983
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721726789.4U Active CN207904186U (en) | 2017-12-12 | 2017-12-12 | Mobile oil-sand in-situ treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207904186U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107892458A (en) * | 2017-12-12 | 2018-04-10 | 长春三真实业有限公司 | Portable greasy filth in-situ treatment device |
| CN109488270A (en) * | 2019-01-09 | 2019-03-19 | 成都聚熵能源科技有限公司 | A kind of system and method for two-way horizontal well hot fume sealing and circulating exploitation oil-sand |
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2017
- 2017-12-12 CN CN201721726789.4U patent/CN207904186U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107892458A (en) * | 2017-12-12 | 2018-04-10 | 长春三真实业有限公司 | Portable greasy filth in-situ treatment device |
| CN109488270A (en) * | 2019-01-09 | 2019-03-19 | 成都聚熵能源科技有限公司 | A kind of system and method for two-way horizontal well hot fume sealing and circulating exploitation oil-sand |
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