CN220098922U - Reaction kettle for oil refining processing - Google Patents
Reaction kettle for oil refining processing Download PDFInfo
- Publication number
- CN220098922U CN220098922U CN202321424839.9U CN202321424839U CN220098922U CN 220098922 U CN220098922 U CN 220098922U CN 202321424839 U CN202321424839 U CN 202321424839U CN 220098922 U CN220098922 U CN 220098922U
- Authority
- CN
- China
- Prior art keywords
- chamber
- finished product
- fixedly connected
- kettle
- kettle body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 31
- 238000007670 refining Methods 0.000 title claims abstract description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 230000017525 heat dissipation Effects 0.000 claims description 11
- 239000002893 slag Substances 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 7
- 238000011049 filling Methods 0.000 claims description 3
- 239000011229 interlayer Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 9
- 230000008569 process Effects 0.000 abstract description 6
- 238000003912 environmental pollution Methods 0.000 abstract description 4
- 239000000945 filler Substances 0.000 abstract description 4
- 239000000446 fuel Substances 0.000 abstract description 3
- 238000009423 ventilation Methods 0.000 abstract description 3
- 238000002156 mixing Methods 0.000 abstract description 2
- 238000005457 optimization Methods 0.000 description 5
- 239000002699 waste material Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 244000309464 bull Species 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model discloses a reaction kettle for oil refining processing, which comprises a kettle body, wherein the front surface of the kettle body is provided with a filler opening, and the top of the kettle body is fixedly connected with a motor frame. According to the utility model, through the arrangement of the u-shaped stirrer and the spiral condensing chamber, the servo motor is started to drive the rotary rod to rotate so that the u-shaped stirrer rotates along with the rotary rod, the u-shaped stirrer is suitable for the processes of mixing, heat transfer or reaction of medium-high viscosity liquid, and the like, horizontal annular flow generated during rotation can increase vortex near the paddles so that stirring is more uniform and sufficient, meanwhile, evaporated steam enters the spiral condensing chamber from the guide pipe to be condensed into liquid oil, residual tail gas which cannot be condensed enters the finished product chamber along with the liquid oil, and then flows into the connecting pipe communicated with the bottom of the finished product chamber through the ventilation hole so as to enter the heating chamber, so that fuel serving as an ignition device is recycled, environmental pollution is not caused, the use of a user is facilitated, and the practicability of the reaction kettle is improved.
Description
Technical Field
The utility model relates to the technical field of oil refining processing, in particular to a reaction kettle for oil refining processing.
Background
The method is characterized in that visible white garbage is filled everywhere in life, several tons of garbage are buried underground, degradation and disappearance can be achieved in a short time, degradation can be achieved in hundreds of years, and particularly, a large amount of toxicity can be generated in the degradation process of the undegradable matters, so that the ground land is free from being planted with trees, and although plastic garbage is produced by people, people can reuse the plastic garbage to eliminate the plastic garbage as much as possible, and a technology called waste plastic oil refining is mentioned.
Waste plastic oil refining is usually recovered by adopting a pyrolysis oil decomposition technology, namely waste plastic is cracked by heating or adding a certain catalyst, and the plastic is heated and melted to become viscous liquid which hinders the stirring blade from fully stirring the stirring blade, so that the stirring is not uniform enough to cause the oil refining efficiency to be difficult to improve, meanwhile, in the process of plastic heating and cracking, part of combustible tail gas but non-condensable tail gas is generated except oil gas, the direct emission can cause environmental pollution, the use of a user is inconvenient, and the practicability of the reaction kettle is reduced.
Disclosure of Invention
In order to solve the problems in the prior art, the utility model aims to provide a reaction kettle for oil refining processing, which has the advantages of uniform stirring and no environmental pollution caused by recycling tail gas, and solves the problems that the stirring blades are blocked by thick liquid which is formed after plastic is heated and melted to sufficiently stir the stirring blades, so that the oil refining efficiency is difficult to improve due to insufficient stirring, and meanwhile, in the process of heating and cracking the plastic, part of combustible but non-condensable tail gas is generated except oil gas, and the environment is polluted due to direct discharge.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a reaction kettle for oil refining processing, includes the cauldron body, the front of the cauldron body is provided with the filler mouth, the top fixedly connected with motor frame of the cauldron body, the inside fixedly connected with servo motor of motor frame, the inside of the cauldron body is provided with reaction chamber and heating chamber respectively, servo motor's output runs through to the inside of reaction chamber and fixedly connected with bull stick, the fixed surface of bull stick is connected with u-shaped agitator, the right side of the cauldron body is provided with the gas pipe, the diapire of heating chamber is provided with ignition, the gas pipe runs through to the inside of heating chamber and communicates with ignition;
the top intercommunication on reaction chamber right side has steam outlet, the top intercommunication of the cauldron body has the pipe, the output intercommunication of pipe has the spiral condensing chamber, the bottom fixedly connected with finished product room of spiral condensing chamber, the output of spiral condensing chamber runs through to the roof of finished product room, the diapire fixedly connected with division board of finished product room, the bleeder vent has been seted up at the top of division board, the left side intercommunication of finished product room has the finished product export, the right side intercommunication of finished product room has the connecting pipe, the connecting pipe runs through to the inside of heating chamber and communicates with the heating chamber.
As a preferable mode of the utility model, heat dissipation convex blocks are arranged around the spiral condensing chamber, and the number of the heat dissipation convex blocks is a plurality.
As preferable in the utility model, the left side and the right side of the u-shaped stirrer are fixedly connected with a plurality of blades.
As preferable mode of the utility model, a labyrinth channel is arranged in the interlayer of the kettle body.
As the preferable mode of the utility model, the left wall of the finished product chamber is fixedly connected with a liquid level sensor, the top of the finished product outlet is provided with an electric control valve, and the liquid level sensor is in signal connection with the electric control valve.
As the preferable mode of the utility model, the back of the kettle body is respectively communicated with a slag discharging port and a water pipe, the input end of the water pipe is communicated with a water pump, and the tops of the slag discharging port and the water pipe are respectively provided with an electric control valve.
Compared with the prior art, the utility model has the following beneficial effects:
1. according to the utility model, through the arrangement of the u-shaped stirrer and the spiral condensing chamber, the servo motor is started to drive the rotary rod to rotate so that the u-shaped stirrer rotates along with the rotary rod, the u-shaped stirrer is suitable for the processes of mixing, heat transfer or reaction of medium-high viscosity liquid, and the like, horizontal annular flow generated during rotation can increase vortex near the paddles so that stirring is more uniform and sufficient, meanwhile, evaporated steam enters the spiral condensing chamber from the guide pipe to be condensed into liquid oil, residual tail gas which cannot be condensed enters the finished product chamber along with the liquid oil, and then flows into the connecting pipe communicated with the bottom of the finished product chamber through the ventilation hole so as to enter the heating chamber, so that fuel serving as an ignition device is recycled, environmental pollution is not caused, the use of a user is facilitated, and the practicability of the reaction kettle is improved.
2. According to the utility model, through the arrangement of the heat dissipation convex blocks, the contact area between the spiral condensing chamber and the air is increased, and the heat dissipation efficiency is improved.
Drawings
FIG. 1 is a schematic elevational cross-sectional view of the structure of the present utility model;
FIG. 2 is a schematic elevational view of the structure of the present utility model;
fig. 3 is a schematic top view of the structure of the present utility model.
In the figure: 1. a kettle body; 2. a filler port; 3. a motor frame; 4. a servo motor; 5. a reaction chamber; 6. a heating chamber; 7. a rotating rod; 8. a u-shaped stirrer; 9. a gas pipe; 10. an ignition device; 11. a steam outlet; 12. a conduit; 13. a spiral condensing chamber; 14. a finished product chamber; 15. a partition plate; 16. ventilation holes; 17. a finished product outlet; 18. a connecting pipe; 19. a heat dissipation bump; 20. a blade; 21. a labyrinth passage; 22. a liquid level sensor; 23. a slag discharge port; 24. a water pipe; 25. and (3) a water pump.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
As shown in fig. 1 to 3, a reaction kettle for oil refining processing comprises a kettle body 1, wherein a filler port 2 is arranged on the front surface of the kettle body 1, a motor frame 3 is fixedly connected to the top of the kettle body 1, a servo motor 4 is fixedly connected to the inside of the motor frame 3, a reaction chamber 5 and a heating chamber 6 are respectively arranged in the kettle body 1, an output end of the servo motor 4 penetrates into the reaction chamber 5 and is fixedly connected with a rotating rod 7, a u-shaped stirrer 8 is fixedly connected to the surface of the rotating rod 7, a gas pipe 9 is arranged on the right side of the kettle body 1, an ignition device 10 is arranged on the bottom wall of the heating chamber 6, and the gas pipe 9 penetrates into the heating chamber 6 and is communicated with the ignition device 10;
the top intercommunication on reaction chamber 5 right side has steam outlet 11, the top intercommunication of the cauldron body 1 has pipe 12, the output intercommunication of pipe 12 has spiral condensing chamber 13, the bottom fixedly connected with finished product room 14 of spiral condensing chamber 13, the output of spiral condensing chamber 13 runs through to the roof of finished product room 14, the diapire fixedly connected with division board 15 of finished product room 14, bleeder vent 16 has been seted up at the top of division board 15, the left side intercommunication of finished product room 14 has finished product export 17, the right side intercommunication of finished product room 14 has connecting pipe 18, connecting pipe 18 runs through to the inside of heating chamber 6 and communicates with heating chamber 6.
Referring to fig. 1, 2 and 3, heat dissipation protrusions 19 are provided around the spiral condensing chamber 13, and the number of the heat dissipation protrusions 19 is several.
As a technical optimization scheme of the utility model, the spiral condensing chamber 13 increases the contact area with air through the arrangement of the heat dissipation convex blocks 19, so that the heat dissipation efficiency is improved.
Referring to fig. 1, blades 20 are fixedly connected to the left and right sides of the u-shaped stirrer 8, and the number of the blades 20 is a plurality.
As a technical optimization scheme of the utility model, through the arrangement of the blades 20, the stirring range is enlarged, so that the stirring is more uniform, and the heating evaporation speed is improved.
Referring to fig. 1, a labyrinth passage 21 is provided in an interlayer of the tank body 1.
As a technical optimization scheme of the utility model, through the arrangement of the labyrinth channel 21, steam is used for keeping the temperature of the kettle body 1 and reducing the temperature of the kettle body, so that the oil refining efficiency is improved.
Referring to fig. 1, a liquid level sensor 22 is fixedly connected to the left wall of the finished product chamber 14, an electric control valve is arranged at the top of the finished product outlet 17, and the liquid level sensor 22 is in signal connection with the electric control valve.
As a technical optimization scheme of the utility model, through the arrangement of the liquid level sensor 22, when the liquid level of the liquid oil reaches the end head of the liquid level sensor 22, the electric control valve is opened to drain the liquid oil into a finished product tank, so that the liquid level is prevented from exceeding the air holes 16 and entering the heating chamber 6.
Referring to fig. 3, the back of the kettle body 1 is respectively communicated with a slag discharging port 23 and a water pipe 24, the input end of the water pipe 24 is communicated with a water pump 25, and the tops of the slag discharging port 23 and the water pipe 24 are respectively provided with an electric control valve.
As a technical optimization scheme of the utility model, the problems that the next use is affected because the slag discharge cleaning work cannot be performed in the reaction chamber 5 after the oil refining work is finished are avoided through the arrangement of the slag discharge port 23, the water pipe 24 and the water pump 25.
The working principle and the using flow of the utility model are as follows: when the device is used, a user opens the filling port 2 to fill waste plastic into the reaction chamber 5 and seals the filling port 2, then starts the ignition device 10 to ignite and burn to continuously heat the bottom of the reaction chamber 5, simultaneously starts the servo motor 4 to enable the rotary rod 7 to rotate to drive the u-shaped stirrer 8 to rotate, and generates horizontal annular flow to increase vortex near the paddle to enable stirring to be more uniform and sufficient when rotating, meanwhile, evaporated steam cools the kettle body 1 while preserving heat, enters the spiral condensation chamber 13 through the guide pipe 12 to condensate liquid oil, finally drops into the finished product chamber 14, residual tail gas which cannot be condensed enters the finished product chamber 14 along with the liquid oil, flows into the connecting pipe 18 communicated with the bottom of the finished product chamber 14 through the air hole 16 to enter the heating chamber 6, fuel serving as the ignition device 10 is recycled, opens the electric valve at the water pipe 24 to enable the water pump 25 to be fed into clear water to flush and stir the reaction chamber 5 after refining is completed, and finally opens the electric valve at the slag discharging port 23 to remove residues.
It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a reation kettle is used in oil refining processing, includes the cauldron body (1), its characterized in that: the novel kettle comprises a kettle body (1), and is characterized in that a filling port (2) is formed in the front face of the kettle body (1), a motor frame (3) is fixedly connected to the top of the kettle body (1), a servo motor (4) is fixedly connected to the inside of the motor frame (3), a reaction chamber (5) and a heating chamber (6) are respectively arranged in the kettle body (1), an output end of the servo motor (4) penetrates through the inside of the reaction chamber (5) and is fixedly connected with a rotating rod (7), a u-shaped stirrer (8) is fixedly connected to the surface of the rotating rod (7), a gas pipe (9) is arranged on the right side of the kettle body (1), an ignition device (10) is arranged on the bottom wall of the heating chamber (6), and the gas pipe (9) penetrates through the inside of the heating chamber (6) and is communicated with the ignition device (10);
the top intercommunication on reaction chamber (5) right side has steam outlet (11), the top intercommunication of cauldron body (1) has pipe (12), the output intercommunication of pipe (12) has spiral condensing chamber (13), the bottom fixedly connected with finished product room (14) of spiral condensing chamber (13), the output of spiral condensing chamber (13) runs through to the roof of finished product room (14), the diapire fixedly connected with division board (15) of finished product room (14), bleeder vent (16) have been seted up at the top of division board (15), the left side intercommunication of finished product room (14) has finished product export (17), the right side intercommunication of finished product room (14) has connecting pipe (18), connecting pipe (18) run through to the inside of heating chamber (6) and with heating chamber (6) intercommunication.
2. The reaction kettle for oil refining processing according to claim 1, wherein: and heat dissipation convex blocks (19) are arranged around the spiral condensing chamber (13), and the number of the heat dissipation convex blocks (19) is a plurality.
3. The reaction kettle for oil refining processing according to claim 1, wherein: blades (20) are fixedly connected to the left side and the right side of the u-shaped stirrer (8), and the number of the blades (20) is a plurality of blades.
4. The reaction kettle for oil refining processing according to claim 1, wherein: the interlayer of the kettle body (1) is provided with a labyrinth channel (21).
5. The reaction kettle for oil refining processing according to claim 1, wherein: the left wall of the finished product chamber (14) is fixedly connected with a liquid level sensor (22), an electric control valve is arranged at the top of the finished product outlet (17), and the liquid level sensor (22) is in signal connection with the electric control valve.
6. The reaction kettle for oil refining processing according to claim 1, wherein: the back of the kettle body (1) is respectively communicated with a slag discharging port (23) and a water pipe (24), the input end of the water pipe (24) is communicated with a water pump (25), and the tops of the slag discharging port (23) and the water pipe (24) are respectively provided with an electric control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321424839.9U CN220098922U (en) | 2023-06-06 | 2023-06-06 | Reaction kettle for oil refining processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321424839.9U CN220098922U (en) | 2023-06-06 | 2023-06-06 | Reaction kettle for oil refining processing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220098922U true CN220098922U (en) | 2023-11-28 |
Family
ID=88867258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321424839.9U Active CN220098922U (en) | 2023-06-06 | 2023-06-06 | Reaction kettle for oil refining processing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220098922U (en) |
-
2023
- 2023-06-06 CN CN202321424839.9U patent/CN220098922U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201968518U (en) | Steam heating type food preparing machine | |
| CN220098922U (en) | Reaction kettle for oil refining processing | |
| CN111013172A (en) | Wiped film evaporator | |
| CN206899986U (en) | A kind of wine box printing equipment | |
| TWM636932U (en) | Organic waste treatment machine | |
| CN212680143U (en) | Leaching device is used in avermectin production | |
| CN213740444U (en) | Stirring device for color asphalt | |
| CN114806765A (en) | Brewing equipment | |
| CN212174948U (en) | Methane tank with good sealing performance | |
| CN204265755U (en) | For combining the CSTR reactor possessed except scum silica frost ability of anaerobism | |
| CN207552146U (en) | A kind of hardly biodegradableorganic | |
| CN207175884U (en) | A kind of municipal sludge processing unit | |
| CN213436265U (en) | Kitchen waste's biodegradable device | |
| CN208250304U (en) | A kind of CSTR anaerobic reactor inclined in type broken shell blender | |
| CN112317526A (en) | Be used for fertile type thermal desorption soil remediation's equipment | |
| CN2856052Y (en) | Complete equipment for marsh gas from excrement | |
| CN206305177U (en) | A kind of kitchen garbage treater | |
| CN215250679U (en) | Horizontal animal fat of environment-friendly smelts jar | |
| CN212157164U (en) | Pyrolysis system | |
| CN220334869U (en) | Boiler condensate water high-low pressure circulation centrifugal recovery device | |
| CN219347469U (en) | Hot-mix asphalt mixing waste heat recycling device | |
| CN211734291U (en) | Edible vegetable oil decoloration equipment | |
| CN215277168U (en) | Compounding heater is used in high tower chemical fertilizer production with preheat function | |
| CN221182551U (en) | Novel yellow phosphorus rinsing refining device | |
| CN220892265U (en) | Feeding device for dry sludge mixed incineration |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |