CN220269793U - Carbonization reaction device - Google Patents
Carbonization reaction device Download PDFInfo
- Publication number
- CN220269793U CN220269793U CN202321534712.2U CN202321534712U CN220269793U CN 220269793 U CN220269793 U CN 220269793U CN 202321534712 U CN202321534712 U CN 202321534712U CN 220269793 U CN220269793 U CN 220269793U
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- Prior art keywords
- cooling
- water
- pipes
- pipeline
- fixed frame
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- 238000003763 carbonization Methods 0.000 title claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 17
- 238000001816 cooling Methods 0.000 claims abstract description 82
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 76
- 238000005086 pumping Methods 0.000 claims description 4
- 239000000565 sealant Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 24
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 12
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 abstract description 7
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000779 smoke Substances 0.000 abstract description 7
- 238000007599 discharging Methods 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- 229910052799 carbon Inorganic materials 0.000 abstract description 4
- 239000002808 molecular sieve Substances 0.000 abstract description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 description 14
- 239000000498 cooling water Substances 0.000 description 12
- 229910002804 graphite Inorganic materials 0.000 description 8
- 239000010439 graphite Substances 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000003723 Smelting Methods 0.000 description 4
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 4
- 229910010271 silicon carbide Inorganic materials 0.000 description 4
- HMDDXIMCDZRSNE-UHFFFAOYSA-N [C].[Si] Chemical compound [C].[Si] HMDDXIMCDZRSNE-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to the technical field of carbon molecular sieves, in particular to a carbonization reaction device, which comprises a pipeline, wherein a cooling assembly for cooling high-temperature plasma gas is arranged in the pipeline, the cooling assembly comprises a water tank and a cooling tank which are arranged on the outer wall of the pipeline, a water pump is arranged at the water outlet end of the water tank, a water pipe is arranged at the output end of the water pump, the other end of the water pipe extends into the cooling tank, a fixed frame is arranged in the pipeline, a plurality of cooling pipes are arranged in the fixed frame, two ends of the cooling pipes extend into the fixed frame and are provided with extension pipes, a centralized pipe is arranged in the water tank and the cooling tank, two centralized pipes extend into the fixed frame, and a collecting frame is arranged at the other end of each centralized pipe. The utility model can cool down the high temperature plasma gas in the discharging process, prevent the high temperature environment from being generated on the smoke outlet after the discharge, prevent the generation of nitric oxide and nitrogen dioxide, and reduce the environmental pollution.
Description
Technical Field
The utility model relates to the technical field of carbon molecular sieves, in particular to a carbonization reaction device.
Background
The carbon molecular sieve is a novel adsorbent developed in seventies of 20 th century, is an excellent nonpolar carbon material, and has elemental carbon as a main component.
According to the high-efficient reacting furnace for silicon carbide smelting that patent document of application number CN201920055493.7 provided, the on-line screen storage device comprises a base, the upper surface of base is provided with the furnace body, the inside of furnace body is provided with the heating storehouse, the inside of heating storehouse is provided with heating mechanism, heating mechanism's inside is provided with the conducting strip, the lower extreme of conducting strip is provided with the heating wire, the lower extreme of heating wire is provided with the insulating piece, be provided with the equipment storehouse on the outer wall of one side of heating storehouse, the inside of equipment storehouse is provided with the temperature controller, and the induction end of temperature controller runs through and extends to the inside of heating storehouse, the inside of temperature controller is provided with bimetallic strip, be provided with the ejector pin on the outer wall of one side of bimetallic strip, one side of ejector pin is provided with the moving contact, the top of moving contact is provided with the static contact, the below of temperature controller sets up at the heater. The temperature controller can control the temperature in the reaction furnace, so that the smelting work of silicon carbide is more efficient.
The high-efficiency reaction furnace for smelting silicon carbide in the patent can play a role in controlling the temperature in the reaction furnace through the temperature controller, so that the smelting work of silicon carbide is more efficient. Most carbonization furnace equipment is a high-temperature graphitizing resistance furnace, direct current is applied to two ends of a graphite tube, when current passes through a graphite heating body, the graphite heating body is heated as a resistor, and the current reaches several thousands to tens of thousands amperes due to lower resistivity of the graphite tube, so that low-voltage large-current heating is caused. In the past, after high-temperature carbonization is carried out on a silicon carbon product by high-temperature plasma gas, the high-temperature plasma gas is discharged from a smoke outlet, but the temperature of the high-temperature plasma gas is still higher during discharge, so that a high-temperature environment is caused to the outside after discharge, nitrogen and oxygen in the air produce nitric oxide in the high-temperature environment, and nitrogen dioxide is generated after the nitric oxide is cooled, so that the environment is polluted.
Disclosure of Invention
The present utility model is directed to a carbonization reaction device, which solves the problems set forth in the background art.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
the utility model provides a carbonization reaction device, includes the pipeline, the inside cooling module that is used for cooling to high temperature plasma gas that is provided with of pipeline, cooling module is including setting up water tank and the cooling case at the pipeline outer wall, the water tank water outlet end is provided with the water pump, the water pump output is provided with the raceway, the raceway other end extends to the cooling incasement, the inside fixed frame that is provided with of pipeline, the inside a plurality of cooling tubes that are provided with of fixed frame, a plurality of cooling tube both ends all extend to in the fixed frame and are provided with the extension pipe, water tank and cooling incasement portion all are provided with the collecting pipe, two in the collecting pipe all extends to the fixed frame, two the collecting pipe other end all is provided with the collecting frame.
As a preferable scheme of the utility model, the water tank and the cooling tank are connected with the outer wall of the pipeline through bolts, and the water pump is connected with the outer wall of the water tank through bolts.
As a preferable scheme of the utility model, the water pumping end of the water pump extends into the water tank, and the water outlet end of the water pump is connected with the water delivery pipe through the sleeve.
As a preferable scheme of the utility model, the fixed frame is connected with the inner wall of the pipeline through bolts and sealant, and a plurality of cooling pipes are connected with the inner wall of the fixed frame in an embedded manner.
As a preferable scheme of the utility model, two collecting pipes and the collecting frame are integrally formed, and two ends of a plurality of cooling pipes are integrally formed with the extension pipe.
As a preferred embodiment of the present utility model, the ends of the extension pipes, which are far away from the cooling pipes, extend into the collecting frame.
As a preferable mode of the utility model, a plurality of cooling pipes are arranged in the fixed frame in a crossing way, and the cooling pipes are contacted with the high-temperature plasma gas.
Compared with the prior art, the utility model has the beneficial effects that: to the problem that proposes among the background art, this application has adopted cooling module, through water circulating system and through the cooling tube for the medium to high temperature plasma gas cools down to set up cooling module at a plurality of positions of pipeline, just cool down it in pipeline to high temperature plasma gas exhaust in-process, make it be normal atmospheric temperature state when discharging, thereby can not produce high temperature environment, thereby prevent the production of nitric oxide and nitrogen dioxide, reduce environmental pollution. The utility model can cool down the high temperature plasma gas in the discharging process, prevent the high temperature environment from being generated on the smoke outlet after the discharge, prevent the generation of nitric oxide and nitrogen dioxide, and reduce the environmental pollution.
Drawings
FIG. 1 is a perspective view of the overall structure of the present utility model;
FIG. 2 is a cross-sectional view of a cooling module of the present utility model;
FIG. 3 is a block diagram of a fixed frame of the present utility model;
fig. 4 is an enlarged view of the portion a of the present utility model.
In the figure: 1. a pipe; 2. a water tank; 3. a water pump; 301. a water pipe; 4. a cooling box; 5. a fixed frame; 6. a cooling tube; 601. an extension tube; 7. a collection frame; 701. and (5) centralizing the pipes.
Detailed Description
The technical solutions of the embodiments of the present utility model will be clearly and completely described below in conjunction with the embodiments of the present utility model, and it is apparent that the described embodiments are only some embodiments of the present utility model, but not all embodiments, and all other embodiments obtained by those skilled in the art without making any inventive effort based on the embodiments of the present utility model are within the scope of protection of the present utility model.
In order that the utility model may be readily understood, a more complete description of the utility model will be rendered by reference to the appended drawings. Several embodiments of the utility model are presented. This utility model may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
It will be understood that when an element is referred to as being "mounted" on another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present. The terms "vertical," "horizontal," "left," "right," and the like are used herein for illustrative purposes only.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this utility model belongs. The terminology used herein in the description of the utility model is for the purpose of describing particular embodiments only and is not intended to be limiting of the utility model. The term "and/or" as used herein includes any and all combinations of one or more of the associated listed items.
Referring to fig. 1-4, the present utility model provides a technical solution: the carbonization reaction device comprises a pipeline 1, a cooling component for cooling high-temperature plasma gas is arranged inside the pipeline 1, the cooling component comprises a water tank 2 and a cooling tank 4 which are arranged on the outer wall of the pipeline 1, the water tank 2 is used for storing cooling water, a cold air machine is arranged in the cooling tank 4 and can cool the cooling water in the cooling tank 4, a water pump 3 is arranged at the water outlet end of the water tank 2 and is used for pumping and conveying the cooling water in the water tank 2 into the cooling tank 4, a water pipe 301 is arranged at the output end of the water pump 3 and is used for conveying the cooling water, the other end of the water pipe 301 extends into the cooling tank 4, a fixed frame 5 is arranged inside the pipeline 1, a plurality of cooling pipes 6 are arranged inside the fixed frame 5 and are made of aluminum materials, the cooling device has good heat conduction performance, the high-temperature plasma gas can be cooled through the cooling pipes 6, the cross design of the cooling pipes 6 can increase the contact with high-temperature plasma gas, thereby increasing the cooling effect, two ends of the cooling pipes 6 extend into the fixed frame 5 and are provided with extension pipes 601 which can extend into the collecting frame 7 and convey cooling water in the cooling pipes 6 to the collecting frame 7, the interiors of the water tank 2 and the cooling box 4 are respectively provided with a collecting pipe 701, the collecting pipes 701 in the water tank 2 are used for conveying and refluxing the cooling water in the corresponding collecting frame 7 into the water tank 2, the collecting pipes 701 in the cooling box 4 can convey the cooling water in the cooling box 4 into the collecting frame 7 and shunt the cooling water into the cooling pipes 6 to realize water circulation, the two collecting pipes 701 extend into the fixed frame 5, the other ends of the two collecting pipes 701 are respectively provided with the collecting frame 7, the cooling assembly is arranged at a plurality of positions of the smoke exhaust pipes, cooling of the high temperature plasma gas may be increased.
Most carbonization furnace equipment is a high-temperature graphitizing resistance furnace, direct current is applied to two ends of a graphite tube, when current passes through a graphite heating body, the graphite heating body is heated as a resistor, and the current reaches several thousands to tens of thousands amperes due to lower resistivity of the graphite tube, so that low-voltage large-current heating is caused. In the past, after high-temperature carbonization is carried out on a silicon carbon product by high-temperature plasma gas, the high-temperature plasma gas is discharged from a smoke outlet, but the temperature of the high-temperature plasma gas is still higher during discharge, so that a high-temperature environment is caused to the outside after discharge, nitrogen and oxygen in the air produce nitric oxide in the high-temperature environment, and nitrogen dioxide is generated after the nitric oxide is cooled, so that the environment is polluted.
All electrical components in this embodiment are controlled by a conventional controller.
Referring to fig. 1-4, the water tank 2 and the cooling tank 4 are connected with the outer wall of the pipeline 1 through bolts, the water pump 3 is connected with the outer wall of the water tank 2 through bolts, the water pumping end of the water pump 3 extends into the water tank 2, the water outlet end of the water pump 3 is connected with the water pipe 301 through a sleeve, the fixed frame 5 is connected with the inner wall of the pipeline 1 through bolts and sealant, a plurality of cooling pipes 6 are connected with the inner wall of the fixed frame 5 in an embedded manner, two collecting pipes 701 and a collecting frame 7 are integrally formed, a plurality of cooling pipes 6 are integrally formed with an extending pipe 601, one end of the extending pipe 601, far from the cooling pipe 6, extends into the collecting frame 7, a plurality of cooling pipes 6 are arranged inside the fixed frame 5 in a crossing manner, and the cooling pipes 6 are contacted with high-temperature plasma gas. When the cooling device is used, the water pump 3 is controlled to operate to convey cooling water in the water tank 2 into the cooling box 4 through the water conveying pipe 301, the cooling water is conveyed into the cooling pipes 6 through the collecting pipes 701 and the collecting frames 7 in the cooling box 4, and meanwhile flows into the collecting frames 7 at the other ends of the cooling pipes 6 and flows back into the water tank 2 through the corresponding collecting pipes 701 to realize water circulation, and when high-temperature plasma gas passes through the cooling pipes 6, the gas can be cooled. The utility model can cool down the high temperature plasma gas in the discharging process, prevent the high temperature environment from being generated on the smoke outlet after the discharge, prevent the generation of nitric oxide and nitrogen dioxide, and reduce the environmental pollution.
The working flow of the utility model is as follows: when the cooling device is used, the water pump 3 is controlled to operate to convey cooling water in the water tank 2 into the cooling box 4 through the water conveying pipe 301, the cooling water is conveyed into the cooling pipes 6 through the collecting pipes 701 and the collecting frames 7 in the cooling box 4, and meanwhile flows into the collecting frames 7 at the other ends of the cooling pipes 6 and flows back into the water tank 2 through the corresponding collecting pipes 701 to realize water circulation, and when high-temperature plasma gas passes through the cooling pipes 6, the gas can be cooled. The utility model can cool down the high temperature plasma gas in the discharging process, prevent the high temperature environment from being generated on the smoke outlet after the discharge, prevent the generation of nitric oxide and nitrogen dioxide, and reduce the environmental pollution.
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 (7)
1. The utility model provides a carbonization reaction device, includes pipeline (1), pipeline (1) inside is provided with the cooling module that is used for cooling down high temperature plasma gas, its characterized in that: the cooling assembly comprises a water tank (2) and a cooling box (4) which are arranged on the outer wall of a pipeline (1), a water pump (3) is arranged at the water outlet end of the water tank (2), a water pipe (301) is arranged at the output end of the water pump (3), the other end of the water pipe (301) extends into the cooling box (4), a fixed frame (5) is arranged inside the pipeline (1), a plurality of cooling pipes (6) are arranged inside the fixed frame (5), a plurality of cooling pipes (6) are respectively arranged at two ends of each cooling pipe (6) and are respectively provided with an extension pipe (601), a centralized pipe (701) is respectively arranged inside the water tank (2) and the cooling box (4), the centralized pipes (701) are respectively arranged in the fixed frame (5), and collecting frames (7) are respectively arranged at the other ends of the centralized pipes (701).
2. A carbonization reaction apparatus according to claim 1, characterized in that: the water tank (2) and the cooling box (4) are connected with the outer wall of the pipeline (1) through bolts, and the water pump (3) is connected with the outer wall of the water tank (2) through bolts.
3. A carbonization reaction apparatus according to claim 1, characterized in that: the water pumping end of the water pump (3) extends into the water tank (2), and the water outlet end of the water pump (3) is connected with the water delivery pipe (301) through a sleeve.
4. A carbonization reaction apparatus according to claim 1, characterized in that: the fixed frame (5) is connected with the inner wall of the pipeline (1) through bolts and sealant, and the cooling pipes (6) are connected with the inner wall of the fixed frame (5) in an embedded mode.
5. A carbonization reaction apparatus according to claim 1, characterized in that: two collecting pipes (701) and a collecting frame (7) are integrally formed, and two ends of a plurality of cooling pipes (6) are integrally formed with an extension pipe (601).
6. A carbonization reaction apparatus according to claim 1, characterized in that: one end of the extension pipe (601) far away from the cooling pipe (6) extends into the collecting frame (7).
7. A carbonization reaction apparatus according to claim 1, characterized in that: the cooling pipes (6) are all arranged in the fixed frame (5) in a cross mode, and the cooling pipes (6) are in contact with high-temperature plasma gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321534712.2U CN220269793U (en) | 2023-06-15 | 2023-06-15 | Carbonization reaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321534712.2U CN220269793U (en) | 2023-06-15 | 2023-06-15 | Carbonization reaction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220269793U true CN220269793U (en) | 2023-12-29 |
Family
ID=89305004
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321534712.2U Active CN220269793U (en) | 2023-06-15 | 2023-06-15 | Carbonization reaction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220269793U (en) |
-
2023
- 2023-06-15 CN CN202321534712.2U patent/CN220269793U/en active Active
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