CN207904183U - A kind of oil-sand separation pyrolysis installation - Google Patents
A kind of oil-sand separation pyrolysis installation Download PDFInfo
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- CN207904183U CN207904183U CN201721726802.6U CN201721726802U CN207904183U CN 207904183 U CN207904183 U CN 207904183U CN 201721726802 U CN201721726802 U CN 201721726802U CN 207904183 U CN207904183 U CN 207904183U
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- heating mantle
- sand
- pyrolysis installation
- sand separation
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Abstract
The utility model is related to a kind of oil-sand separation pyrolysis installations, including：Heating mantle, left end are equipped with feed inlet, and right end is equipped with discharge port；Heated mandrel, is arranged the center in the heating mantle, and both ends are connected to by the first connection section and the second connection section with the both ends of the heating mantle respectively；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 passed through from the air inlet, and being circulated to the gas outlet by heating mantle and heated mandrel is discharged.The oil-sand separation pyrolysis installation of the utility model is integrally carried out while being heated to pyrolysis installation by high-temperature fuel gas, realize 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.
Description
Technical field
The utility model is related to a kind of separating and treating apparatus, more particularly to a kind of oil-sand separation pyrolysis installation.
Background technology
Oil-sand resource very abundant in the world is much larger than the proved reserves of oil.Oil-sand is rear stone as unconventional energy resource
The alternative energy source of most realistic meaning of oily epoch will play the role of very important in world's energy resource supply.Develop oil-sand
Resource meets national energy policy, to ensuring that the energy security in China has great importance.
There are mainly three types of current oil-sand treatment technologies：Hot water wash partition method, solution extraction and hot cracking process.Wherein,
Temperature height needed for hot cracking process, energy consumption are larger, but the lightweight oil-sand quality after cracking is preferable.Application heat in the prior art
The oil-sand separation pyrolysis installation of cracking process is as shown in Figure 1 comprising a pyrolysis oven 101,101 top of pyrolysis oven are equipped with charging
Mouth 104, lower part are equipped with discharge port 105, are internally provided with auger 102.The auger 102 is used for pending by feed inlet 104
The oil-sand of entrance is delivered to discharge port 105, and pyrolysis oven 101 is discharged.The lower section of pyrolysis oven 101 is equipped with heating device 103, leads to
Burning fuel is crossed to heat pyrolysis oven 101.
Above-mentioned oil-sand separation pyrolysis installation the problem is that：Equipment volume is huge, and construction cost is high, can not be in all oil
Build respectively to sand resource；Heating device is low for the efficiency of heating surface of pyrolysis oven, greatly reduces pyrolysis efficiency.
Utility model content
The technical issues of the utility model will solve in the prior art provides a kind of oil-sand separation pyrolysis installation.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is specific as follows：
A kind of oil-sand separation pyrolysis installation, including：
Heating mantle, left end are equipped with feed inlet, and right end is equipped with discharge port；
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 1
Rotation, push oil-sand move from left to right.
In the above-mentioned technical solutions, the heated mandrel outer wall is equipped with multiple interior pushing sheets, can be with the heated mandrel
Rotation, push oil-sand move from left to right.
In the above-mentioned technical solutions, the heating mantle and the heated mandrel are internally provided with multiple labyrinth catch, labyrinth gear
Piece can delay passing through for high-temperature fuel gas.
In the above-mentioned technical solutions, the top of the outer pushing sheet and interior pushing sheet is equipped with " L " shape structure.
The utility model has advantageous effect below：
The oil-sand separation pyrolysis installation of the utility model is integrally carried out while being heated to pyrolysis installation by high-temperature fuel gas,
The high-efficiency thermal decomposition for realizing oil-sand greatly reduces the volume and weight of pyrolysis installation and is moved so that it can be placed on truck
Work.
The oil-sand separation pyrolysis installation of the utility model, labyrinth catch is respectively equipped in heating mantle and heated mandrel, is played
Delay effect of the high-temperature fuel gas by speed, further improves the efficiency of heating surface.
The oil-sand separation pyrolysis installation of the utility model, by be respectively set in heating mantle and heated mandrel outer pushing sheet and
Interior pushing sheet 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 the structural schematic diagram of oil-sand separation pyrolysis installation in the prior art.
Fig. 2 is the structural schematic diagram of the oil-sand separation pyrolysis installation of the utility model.
Fig. 3 is the A-A of oil-sand separation pyrolysis installation shown in Fig. 2 to schematic cross-section.
Reference numeral in figure is expressed as：
101- pyrolysis ovens；102- augers；103- heating devices；104- feed inlets；105- discharge ports；
1- heating mantles；The outer pushing sheets of 2-；Pushing sheet in 3-；4- heated mandrels；The labyrinths 5- catch；6- air inlets；The gas outlets 7-；
The connection sections of 8- first；The connection sections of 9- second.
Specific implementation mode
The utility model thought of the utility model is：The oil-sand separation pyrolysis installation of the utility model improves oil-sand and heat
The heat exchanger effectiveness for solving device, realizes the high-efficiency thermal decomposition of oil-sand, greatly reduces the volume and weight of pyrolysis installation.
The utility model is described in detail below in conjunction with the accompanying drawings.
As shown in Figures 2 and 3, the oil-sand separation pyrolysis installation of the utility model includes：Heating mantle 1 and heated mandrel 4.Heating mantle
1 left end is equipped with feed inlet, and right end is equipped with discharge port, is respectively intended to add pending oil-sand raw material and discharge treated oil
Sand.Inlet port and outlet port are not shown in FIG. 2.The center in the heating mantle 1, both ends are arranged in heated mandrel 4
It is connected to respectively with the both ends of the heating mantle 1 by the first connection section 8 and the second connection section 9.As shown in Fig. 2, 1 inner wall of heating mantle
It is equipped with multiple outer pushing sheets 2,4 outer wall of heated mandrel is equipped with multiple interior pushing sheets 3, and outer pushing sheet 2 and interior pushing sheet 3 can be with
With the rotation of heating mantle 1, oil-sand is pushed to move from left to right.
First connection section 8 is connected with air inlet 6, and the second connection section 9 is connected with gas outlet 7；High-temperature fuel gas can from it is described into
Gas port 6 is passed through, and being circulated to the gas outlet 7 by heating mantle 1 and heated mandrel 4 is discharged.Heating mantle 1 and heated mandrel 4 are internally provided with
Multiple labyrinth catch 5, the labyrinth catch 5 can delay passing through for high-temperature fuel gas, and then play the role of improving heat exchanger effectiveness.
During the work time, high-temperature fuel gas is passed through the oil-sand separation pyrolysis installation of the utility model by the air inlet 6 on right side
In first connection section 8, the conducting Jing Guo heating mantle 1 and heated mandrel 4 respectively later is sent at the second connection section 9 in left side, it
It is discharged again by gas outlet 7 afterwards.High-temperature fuel gas realizes the heating to heating mantle 1 and heated mandrel 4 in above-mentioned conductive process, into
And realize the heating to being connected to outer pushing sheet 2 and interior pushing sheet 3 in heating mantle 1 and heated mandrel 4.In outer pushing sheet
2 and interior pushing sheet 3 push oil-sand when moving from left to right, sufficient heating just has been carried out to oil-sand.As shown in figure 3, outer pusher
Piece 2 and interior pushing sheet 3 are equipped with L-shaped structure on top, during pushing oil-sand to advance, play the work for stirring oil-sand
With more fully realizing the heat exchange between oil-sand.
The inside of heating mantle 1 and heated mandrel 4 further respectively has labyrinth catch 5, which is delaying high-temperature fuel gas
By while, sufficient heat exchange has been carried out with high-temperature fuel gas, so that heating mantle 1 and heated mandrel 4 have obtained high temperature combustion
The abundant heating of gas.To which the inner wall of heating mantle 1 and the outer wall of heated mandrel 4 can also fill the oil-sand in progradation
The heating divided.
The oil-sand separation pyrolysis installation of the utility model is integrally carried out while being heated to pyrolysis installation by high-temperature fuel gas,
The high-efficiency thermal decomposition for realizing oil-sand greatly reduces the volume and weight of pyrolysis installation and is moved so that it can be placed on truck
Work.
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 (6)
1. a kind of oil-sand separation pyrolysis installation, which is characterized in that including：
Heating mantle (1), left end are equipped with feed inlet, and right end is equipped with discharge port；
Heated mandrel (4), is arranged center in the heating mantle (1), and (8) and the are saved in both ends by the first connection respectively
Two connection sections (9) are connected to the both ends of the heating mantle (1)；
The first connection section (8) is connected with air inlet (6), and the second connection section (9) is connected with gas outlet (7)；High temperature fires
Gas can be passed through from the air inlet (6), and the gas outlet (7) discharge is circulated to by heating mantle (1) and heated mandrel (4).
2. oil-sand separation pyrolysis installation according to claim 1, which is characterized in that heating mantle (1) inner wall is equipped with
Multiple outer pushing sheets (2) can push oil-sand to move from left to right with the rotation of the heating mantle (1).
3. oil-sand separation pyrolysis installation according to claim 1, which is characterized in that heated mandrel (4) outer wall is equipped with
Multiple interior pushing sheets (3) can push oil-sand to move from left to right with the rotation of the heated mandrel (4).
4. oil-sand separation pyrolysis installation according to claim 1, which is characterized in that the heating mantle (1) and the heating
Axis (4) is internally provided with multiple labyrinth catch (5), which can delay passing through for high-temperature fuel gas.
5. oil-sand separation pyrolysis installation according to claim 2, which is characterized in that the top of the outer pushing sheet (2) is set
There is " L " shape structure.
6. oil-sand separation pyrolysis installation according to claim 3, which is characterized in that the top of the interior pushing sheet (3) is set
There is " L " shape structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721726802.6U CN207904183U (en) | 2017-12-12 | 2017-12-12 | A kind of oil-sand separation pyrolysis installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721726802.6U CN207904183U (en) | 2017-12-12 | 2017-12-12 | A kind of oil-sand separation pyrolysis installation |
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| Publication Number | Publication Date |
|---|---|
| CN207904183U true CN207904183U (en) | 2018-09-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721726802.6U Active CN207904183U (en) | 2017-12-12 | 2017-12-12 | A kind of oil-sand separation pyrolysis installation |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107892934A (en) * | 2017-12-12 | 2018-04-10 | 长春三真实业有限公司 | A kind of oil-sand separation pyrolysis installation |
| CN109575963A (en) * | 2018-12-20 | 2019-04-05 | 中国重型机械研究院股份公司 | A kind of high-efficiency heat exchanger and its application method for oil-sand pyrolysis |
| CN109575963B (en) * | 2018-12-20 | 2024-06-04 | 中国重型机械研究院股份公司 | Efficient heat exchange device for oil sand pyrolysis and application method thereof |
-
2017
- 2017-12-12 CN CN201721726802.6U patent/CN207904183U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107892934A (en) * | 2017-12-12 | 2018-04-10 | 长春三真实业有限公司 | A kind of oil-sand separation pyrolysis installation |
| CN109575963A (en) * | 2018-12-20 | 2019-04-05 | 中国重型机械研究院股份公司 | A kind of high-efficiency heat exchanger and its application method for oil-sand pyrolysis |
| CN109575963B (en) * | 2018-12-20 | 2024-06-04 | 中国重型机械研究院股份公司 | Efficient heat exchange device for oil sand pyrolysis and application method thereof |
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