CN213746781U - Three-chamber RTO exchange heat accumulation type waste gas incineration device - Google Patents
Three-chamber RTO exchange heat accumulation type waste gas incineration device Download PDFInfo
- Publication number
- CN213746781U CN213746781U CN202022169529.XU CN202022169529U CN213746781U CN 213746781 U CN213746781 U CN 213746781U CN 202022169529 U CN202022169529 U CN 202022169529U CN 213746781 U CN213746781 U CN 213746781U
- Authority
- CN
- China
- Prior art keywords
- rto
- butterfly valve
- pneumatic switching
- chamber
- switching butterfly
- 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
- 239000002912 waste gas Substances 0.000 title claims abstract description 45
- 238000009825 accumulation Methods 0.000 title claims abstract description 18
- 239000007789 gas Substances 0.000 claims abstract description 27
- 238000005338 heat storage Methods 0.000 claims abstract description 23
- 238000011084 recovery Methods 0.000 claims abstract description 16
- 239000002918 waste heat Substances 0.000 claims abstract description 12
- 238000004140 cleaning Methods 0.000 claims description 16
- 238000007664 blowing Methods 0.000 claims description 15
- 238000010926 purge Methods 0.000 claims description 13
- 239000000919 ceramic Substances 0.000 claims description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 230000001172 regenerating effect Effects 0.000 claims 5
- 238000010276 construction Methods 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 abstract description 18
- 230000006378 damage Effects 0.000 abstract description 5
- 239000010815 organic waste Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000004880 explosion Methods 0.000 description 6
- 238000013022 venting Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000007639 printing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002277 temperature effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Images
Landscapes
- Incineration Of Waste (AREA)
Abstract
The utility model relates to a device is burned to three room RTO exchange heat accumulation formula waste gas, including three room RTO, pneumatic switching butterfly valve and waste heat recovery device, the top of three room RTO is installed respectively and is connected to let out and explode valve an and let out and explode valve b, and the internally mounted of three room RTO has the combustor, and the bottom of three room RTO includes 1 room RTO, 2 rooms RTO and 3 rooms RTO, and the 1 room RTO of three room RTO, 2 rooms RTO and 3 rooms RTO export tip are connected pneumatic switching butterfly valve d respectively, pneumatic switching butterfly valve e and pneumatic switching butterfly valve f. The utility model ensures that no bias flow and dead angle can be generated when the waste gas is burnt, and the destruction removal rate of organic matters reaches more than 99.99 percent; the heat storage efficiency of the furnace body is greatly improved; the exhaust gas can be led in a plug flow mode, and the problem of low temperature area formed by overlarge local power when the exhaust gas is led in is avoided; according to the temperature state of the waste gas source in the combustion chamber, whether the combustion chamber is in a safe combustion state or not is judged through thermocouple real-time feedback.
Description
Technical Field
The utility model relates to a waste gas burns device, in particular to three room RTO exchange heat accumulation formula waste gas burns device.
Background
General heat accumulation incinerator can appear bias flow, dead angle problem when waste gas burns, and the organic matter destroys the efficiency of getting rid of not high, and the heat accumulation effect in the furnace body is general simultaneously, and waste gas burns easily incompletely just gets into heat recovery equipment, does not have corresponding thermocouple automatic monitoring temperature effect, can not ensure that waste gas burns thoroughly, and the safety protection effect is not good enough.
Disclosure of Invention
The utility model aims to solve the technical problem of overcoming the defects of the prior art and provides a three-chamber RTO exchange heat accumulation type waste gas incineration device, which ensures that no bias flow and dead angle are generated during waste gas incineration, and ensures that the organic matter destruction removal rate reaches more than 99.99 percent; the heat storage efficiency of the furnace body is greatly improved, and the energy-saving effect of the equipment is obviously improved; the exhaust gas can be led in a plug flow mode, and can slowly and uniformly pass through the vertical high-temperature flame layer, so that the problem of low-temperature area formation caused by overlarge local power when the exhaust gas is led in is avoided; according to the temperature state of the waste gas source in the combustion chamber, whether the combustion chamber is in a safe combustion state or not is judged through thermocouple real-time feedback.
In order to solve the technical problem, the utility model provides a following technical scheme:
the utility model relates to a three room RTO exchange heat accumulation formula waste gas incineration device, including three room RTO, pneumatic switching butterfly valve and waste heat recovery device, a serial communication port, the top of three room RTO is installed respectively and is connected to let out and explode valve an and let out and explode valve b, the internally mounted of three room RTO has the combustor, the bottom of three room RTO includes 1 room RTO, 2 rooms RTO and 3 rooms RTO, install thermocouple c on the top house steward way that 1 room RTO, 2 rooms RTO and 3 rooms RTO are connected, pneumatic switching butterfly valve includes pneumatic switching butterfly valve a, pneumatic switching butterfly valve b, pneumatic switching butterfly valve c, pneumatic switching butterfly valve d, pneumatic switching butterfly valve e and pneumatic switching butterfly valve f, wherein pneumatic switching butterfly valve a, pneumatic switching butterfly valve b, pneumatic switching butterfly valve c connect gradually respectively on one of them waste gas source intake pipe way of 1 room RTO, 2 rooms RTO and 3 rooms RTO, pneumatic switching butterfly valve a, pneumatic switching butterfly valve b, pneumatic switching valve c, The waste gas source air inlet end of the pneumatic switching butterfly valve b and the pneumatic switching butterfly valve c which are connected in series is provided with a filter a, the top end of the filter a is connected with a pressure controller a, the outlet end of the filter a is connected with a draught fan, an air volume controller a is connected on the draught fan in parallel, a thermocouple a is connected on a connecting pipeline between the outlet end of the draught fan and the pneumatic switching butterfly valve a, another waste gas source air inlet pipeline of a 1-room RTO, a 2-room RTO and a 3-room RTO of the three-room RTO is respectively and sequentially connected with a blowing valve a, a blowing valve b and a blowing valve c, the fresh air source air inlet end of the blowing valve a, the blowing valve b and the blowing valve c which are connected in series is provided with a filter b, the top end of the filter b is connected with the pressure controller b, the outlet end of the filter b is connected with a cleaning fan, the air volume controller b is connected on the cleaning fan in parallel, and the connecting pipeline between the outlet end of the cleaning fan and the blowing valve a is connected with the thermocouple b, the end parts of outlets of a chamber 1 RTO, a chamber 2 RTO and a chamber 3 RTO of the three-chamber RTO are respectively connected with a pneumatic switching butterfly valve d, a pneumatic switching butterfly valve e and a pneumatic switching butterfly valve f, a thermocouple d is connected on a pipeline in series connection with the pneumatic switching butterfly valve d, the pneumatic switching butterfly valve e and the pneumatic switching butterfly valve f, the end part of the thermocouple d is connected with a waste heat recovery device, the end part of the waste heat recovery device is connected with a chimney, and the outer side of the chimney is connected with the thermocouple e.
As the utility model discloses a preferred technical scheme of three room RTO exchange heat accumulation formula waste gas incineration device, three room RTO is the venturi type furnace structure.
As the utility model discloses a preferred technical scheme of three room RTO exchange heat accumulation formula waste gas incineration device, all be provided with the heat accumulation bed in 1 room RTO, 2 rooms RTO and the 3 room RTO of three room RTO, the heat accumulation bed is made by pottery.
As the utility model discloses a preferred technical scheme of three room RTO exchange heat accumulation formula waste gas incineration device, 1 room RTO, 2 rooms RTO and 3 rooms RTO furnace exit of three room RTO all are provided with honeycomb heat accumulation wall.
As the utility model discloses a preferred technical scheme of three room RTO exchange heat accumulation formula waste gas incineration device, the air inlet tip that waste gas source is connected to filter an adopts stainless steel spiral waste gas nozzle.
Compared with the prior art, the beneficial effects of the utility model are as follows:
the utility model ensures that no bias flow and dead angle can be generated when the waste gas is burnt, and the destruction removal rate of organic matters reaches more than 99.99 percent; the heat storage efficiency of the furnace body is greatly improved, and the energy-saving effect of the equipment is obviously improved; the exhaust gas can be led in a plug flow mode, and can slowly and uniformly pass through the vertical high-temperature flame layer, so that the problem of low-temperature area formation caused by overlarge local power when the exhaust gas is led in is avoided; according to the temperature state of the waste gas source in the combustion chamber, whether the combustion chamber is in a safe combustion state or not is judged through thermocouple real-time feedback.
Drawings
The accompanying drawings are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention, and together with the description serve to explain the invention and not to limit the invention. In the drawings:
FIG. 1 is an overall structure of the present invention;
in the figure: 1. pneumatically switching a butterfly valve a; 2. a butterfly valve b is switched pneumatically; 3. a butterfly valve c is switched pneumatically; 4. a butterfly valve d is switched pneumatically; 5. a butterfly valve e is switched pneumatically; 6. pneumatically switching a butterfly valve f; 7. a purge valve a; 8. a purge valve b; 9. a purge valve c; 10. three-chamber RTO; 11. a burner; 12. a explosion relief valve a; 13. a explosion venting valve b; 14. a heat storage bed; 15. a chimney; 16. a filter a; 17. a filter b; 18. an induced draft fan; 19. cleaning a fan; 20. a pressure controller a; 21. a pressure controller b; 22. an air volume controller a; 23. an air volume controller b; 24. a thermocouple a; 25. a thermocouple b; 26. a thermocouple c; 27. a thermocouple d; 28. a thermocouple e; 29. a waste heat recovery device.
Detailed Description
The preferred embodiments of the present invention will be described in conjunction with the accompanying drawings, and it will be understood that they are presented herein only to illustrate and explain the present invention, and not to limit the present invention. Wherein like reference numerals refer to like parts throughout.
In addition, if a detailed description of the known art is not necessary to show the features of the present invention, it is omitted. It should be noted that the terms "front," "back," "left," "right," "upper" and "lower" used in the following description refer to directions in the drawings, and the terms "inner" and "outer" refer to directions toward and away from, respectively, the geometric center of a particular component.
Example 1
As shown in fig. 1, the utility model provides a three room RTO exchange heat accumulation formula waste gas incineration device, including three room RTO10, pneumatic switching butterfly valve and waste heat recovery device 29, a serial communication port, the top of three room RTO10 is installed respectively and is connected to let out and explode valve a12 and let out and explode valve b13, the internally mounted of three room RTO10 has combustor 11, the bottom of three room RTO10 contains 1 room RTO, 2 room RTO and 3 room RTO, 1 room RTO, install thermocouple c26 on the top manifold way that 2 room RTO and 3 room RTO are connected, pneumatic switching butterfly valve contains pneumatic switching butterfly valve a1, pneumatic switching butterfly valve b2, pneumatic switching butterfly valve c3, pneumatic switching butterfly valve d4, pneumatic switching butterfly valve e5 and pneumatic switching f6, wherein pneumatic switching butterfly valve a1, pneumatic switching butterfly valve b2, pneumatic switching butterfly valve c3 is connected in proper order respectively at 1 room RTO, one of them waste gas source intake pipe of 2 room RTO and 3 room RTO, pneumatic switching butterfly valve b1 a1 on the way, pneumatic switching butterfly valve, A filter a16 is arranged at the inlet end of the waste gas source, the top end of the filter a16 is connected with a pressure controller a20, the outlet end of the filter a16 is connected with an induced draft fan 18, an air volume controller a22 is connected in parallel on the induced draft fan 18, a thermocouple a24 is connected on a connecting pipeline between the outlet end of the induced draft fan 18 and the pneumatic switching butterfly valve a1, another waste gas source inlet pipeline of the three-chamber RTO10, the 1-chamber RTO, the 2-chamber RTO and the 3-chamber RTO is respectively connected with a purge valve a7, a purge valve b8 and a purge valve c9 in sequence, a filter b17 is arranged at the inlet end of the waste gas source, the fresh air valve b8 and the purge valve c9 are connected in series, the top end of the filter b17 is connected with a pressure controller b21, the outlet end of the filter b17 is connected with a purge fan 19, an air volume controller b23 is connected in parallel on the fan 19, and a connecting pipeline 25 is connected with a connecting pipeline, the end parts of outlets of a 1-chamber RTO, a 2-chamber RTO and a 3-chamber RTO of the three-chamber RTO10 are respectively connected with a pneumatic switching butterfly valve d4, a pneumatic switching butterfly valve e5 and a pneumatic switching butterfly valve f6, a thermocouple d27 is connected to a pipeline in which the pneumatic switching butterfly valve d4, the pneumatic switching butterfly valve e5 and the pneumatic switching butterfly valve f6 are connected in series, the end part of the thermocouple d27 is connected with a waste heat recovery device 29, the end part of the waste heat recovery device 29 is connected with a chimney 15, and the outer side of the chimney 15 is connected with a thermocouple e 28.
Furthermore, the three-chamber RTO10 is of a Venturi furnace structure, so that bias flow and dead angles can not occur during waste gas incineration, and the organic matter destruction removal rate can reach more than 99.99%.
The 1-chamber RTO, the 2-chamber RTO and the 3-chamber RTO of the three-chamber RTO10 are all provided with heat storage beds 14, the heat storage beds 14 are made of ceramics, high-temperature gas generated by oxidation flows through a specially-made ceramic heat storage body, so that the temperature of the ceramic body is raised to realize heat storage, and the heat storage is used for preheating subsequent entering organic waste gas.
The honeycomb structure heat storage walls are arranged at the outlets of the 1-chamber RTO, the 2-chamber RTO and the 3-chamber RTO of the three-chamber RTO10, so that the heat storage efficiency of the furnace body is greatly improved, the energy-saving effect of the device is obviously improved, and meanwhile, the waste gas is prevented from entering the heat recovery device to burn due to incomplete combustion in the furnace cavity.
The end part of the filter a16, which is connected with the gas inlet of the waste gas source, adopts a stainless steel spiral waste gas nozzle, so that the waste gas can be fed in a plug flow mode, the waste gas can slowly and uniformly pass through a vertical high-temperature flame layer, and the problem of low-temperature area caused by overlarge local power when the waste gas is fed is avoided.
Specifically, the pressure controller a20, the pressure controller b21, the air volume controller a22, the air volume controller b23 and the five thermocouple parts 24, 25, 26, 27 and 28 are all externally connected with a computer controller, wherein the explosion venting valve a21, the explosion venting valve b22 and the thermocouple a24 are electrically connected, and whether the combustion chamber is in a safe incineration state or not can be judged through real-time feedback of the thermocouple 24 according to the temperature state of an exhaust gas source during incineration in the combustion chamber.
The device flows high-temperature gas generated by oxidation through a specially-made ceramic heat accumulator 14, so that the ceramic body is heated to store heat, and the heat is used for preheating subsequently-entering organic waste gas. Thereby saving fuel consumption for exhaust gas temperature rise. The ceramic heat storage bed is divided into three beds, each heat storage chamber is sequentially subjected to a heat storage circulation program to perform heat release circulation program work, the heat storage working procedure and the heat release working procedure are controlled by a pneumatic switching butterfly valve a1, a pneumatic switching butterfly valve b2, a pneumatic switching butterfly valve c3, a pneumatic switching butterfly valve d4, a pneumatic switching butterfly valve e5 and a pneumatic switching butterfly valve f6, and the cleaning working procedure is controlled by a cleaning valve a7, a cleaning valve b8 and a cleaning valve c9 to perform repeated and continuous work. After the heat storage chamber is heated, a proper amount of clean fresh air is introduced immediately to clean the heat storage chamber by utilizing the action of the cleaning fan 19 (so as to ensure that the VOC removal rate is more than 98%), and the heat storage process can be started only after the heat storage chamber is cleaned. The clean gas after the continuous cycle working treatment is discharged from the chimney 15 at high altitude.
The technology utilizes the action of a draught fan 18 to preheat organic waste gas through a heat storage bed 14, then the organic waste gas is sent into a combustion chamber to be heated by a combustor 11, the organic waste gas is directly oxidized and decomposed into CO2 and H2O after reaching a high temperature condition, thereby treating waste gas pollutants, and the heat generated during decomposition is recovered by a waste heat recovery device 29, so that the energy-saving environment-friendly device for treating the organic waste gas with medium and high concentration is provided. The device has adopted advanced heat exchange technology and novel honeycomb ceramic heat accumulation material, and high-efficient advanced heat transfer system has guaranteed the effective recovery of oxidative decomposition heat, and the rate of heat recovery is more than 95%, and VOC purification rate is more than 99%, has very big technical advantage in organic waste gas purification field, and the wide application is in trades such as oil, chemical industry, rubber, paint, application, furniture, printing iron ladle, printing.
In the device, a pressure controller a20, a pressure controller b21, an air volume controller a22, an air volume controller b23 and five thermocouples ( parts 24, 25, 26, 27 and 28) are externally connected with a computer controller, wherein an explosion venting valve a21, an explosion venting valve b22 and a thermocouple a24 are electrically connected, and whether the combustion chamber is in a safe incineration state or not is judged through real-time feedback of the thermocouple 24 according to the temperature state of an exhaust gas source during incineration in the combustion chamber, so that the safety performance of the whole device is improved. The apparatus cycle sequence of repeated operation is as follows:
(for convenience in reference to the drawings, the switching valves are identified by reference numerals for the various elements below)
Sequence 1: the pneumatic switching butterfly valves 1 and 6 are opened, the blowing and cleaning valve 8 is opened, and the other pneumatic switching butterfly valves 2, 3, 4 and 5 and the blowing and cleaning valves 7 and 9 are closed;
sequence 2: the pneumatic switching butterfly valves 2 and 4 are opened, the blowing and cleaning valve 9 is opened, and the other pneumatic switching butterfly valves 1, 3, 5 and 6 and the blowing and cleaning valves 7 and 8 are closed;
sequence 3: the pneumatic switching butterfly valves 3 and 5 are opened, the purge valve 7 is opened, and the other pneumatic switching butterfly valves 1, 2, 4 and 6 and the purge valves 8 and 9 are closed.
The utility model ensures that no bias flow and dead angle can be generated when the waste gas is burnt, and the destruction removal rate of organic matters reaches more than 99.99 percent; the heat storage efficiency of the furnace body is greatly improved, and the energy-saving effect of the equipment is obviously improved; the exhaust gas can be led in a plug flow mode, and can slowly and uniformly pass through the vertical high-temperature flame layer, so that the problem of low-temperature area formation caused by overlarge local power when the exhaust gas is led in is avoided; according to the temperature state of the waste gas source in the combustion chamber, whether the combustion chamber is in a safe combustion state or not is judged through the real-time feedback of the thermocouple 24.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described in the foregoing embodiments, or equivalents may be substituted for elements thereof. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (5)
1. The utility model provides a three room RTO exchange heat accumulation formula waste gas incineration device, includes three room RTO (10), pneumatic switching butterfly valve and waste heat recovery device (29), its characterized in that, the top of three room RTO (10) is installed respectively and is connected and is let out and explode valve a (12) and let out and explode valve b (13), the internally mounted of three room RTO (10) has combustor (11), the bottom of three room RTO (10) includes 1 room RTO, 2 room RTO and 3 room RTO, install thermocouple c (26) on the top main pipeline that 1 room RTO, 2 room RTO and 3 room RTO are connected, pneumatic switching butterfly valve contains pneumatic switching butterfly valve a (1), pneumatic switching butterfly valve b (2), pneumatic switching butterfly valve c (3), pneumatic switching butterfly valve d (4), pneumatic switching butterfly valve e (5) and pneumatic switching butterfly valve f (6), wherein pneumatic switching butterfly valve a (1), pneumatic switching butterfly valve b (2), The pneumatic switching butterfly valve c (3) is respectively connected to one of the waste gas source air inlet pipelines of the 1-chamber RTO, the 2-chamber RTO and the 3-chamber RTO in sequence, a filter a (16) is arranged at the waste gas source air inlet end of the pneumatic switching butterfly valve a (1), the pneumatic switching butterfly valve b (2) and the pneumatic switching butterfly valve c (3) which are connected in series, the top end of the filter a (16) is connected with a pressure controller a (20), the outlet end of the filter a (16) is connected with a draught fan (18), the draught fan (18) is connected with an air volume controller a (22) in parallel, a thermocouple a (24) is connected on a connecting pipeline between the outlet end of the draught fan (18) and the pneumatic switching butterfly valve a (1), another waste gas source air inlet pipeline of the 1-chamber RTO, the 2-chamber RTO and the 3-chamber RTO of the three-chamber RTO (10) is respectively connected with a purge valve a (7), a purge valve b (8) and a purge valve c (9) in sequence, a filter b (17) is arranged at the air inlet end of a fresh air source with the blowing valve a (7), the blowing valve b (8) and the blowing valve c (9) connected in series, the top end of the filter b (17) is connected with a pressure controller b (21), the outlet end of the filter b (17) is connected with a cleaning fan (19), an air volume controller b (23) is connected on the cleaning fan (19) in parallel, a thermocouple b (25) is connected on a connecting pipeline between the outlet end of the cleaning fan (19) and the blowing valve a (7), the outlet ends of a 1-chamber RTO, a 2-chamber RTO and a 3-chamber RTO of the three-chamber RTO (10) are respectively connected with a pneumatic switching butterfly valve d (4), a pneumatic switching butterfly valve e (5) and a pneumatic switching butterfly valve f (6), and a thermocouple d (27) is connected on a pipeline with the pneumatic switching butterfly valve d (4), the pneumatic switching butterfly valve e (5) and the pneumatic switching butterfly valve f (6) connected in series, the end part of the thermocouple d (27) is connected with a waste heat recovery device (29), the end part of the waste heat recovery device (29) is connected with a chimney (15), and the outer side of the chimney (15) is connected with a thermocouple e (28).
2. A three-chamber RTO exchange regenerative exhaust gas incineration device according to claim 1, characterised in that the three-chamber RTO (10) is of a venturi furnace construction.
3. A three-chamber RTO exchange regenerative exhaust gas incineration device according to claim 1, characterised in that a heat storage bed (14) is provided in each of the 1-chamber RTO, the 2-chamber RTO and the 3-chamber RTO of the three-chamber RTO (10), and the heat storage bed (14) is made of ceramics.
4. A three-chamber RTO exchange regenerative waste gas incinerator according to claim 3, wherein the 1-chamber RTO, 2-chamber RTO and 3-chamber RTO furnace outlets of said three-chamber RTO (10) are all provided with honeycomb structure regenerative walls.
5. A three-chamber RTO exchange regenerative exhaust gas incineration device according to claim 1, characterised in that the filter a (16) is connected to the inlet end of the exhaust gas source by a stainless steel spiral exhaust gas nozzle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022169529.XU CN213746781U (en) | 2020-09-28 | 2020-09-28 | Three-chamber RTO exchange heat accumulation type waste gas incineration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022169529.XU CN213746781U (en) | 2020-09-28 | 2020-09-28 | Three-chamber RTO exchange heat accumulation type waste gas incineration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213746781U true CN213746781U (en) | 2021-07-20 |
Family
ID=76847157
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022169529.XU Active CN213746781U (en) | 2020-09-28 | 2020-09-28 | Three-chamber RTO exchange heat accumulation type waste gas incineration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213746781U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114427687A (en) * | 2022-03-02 | 2022-05-03 | 山西亚乐士环保技术股份有限公司 | High-temperature low-oxygen heat accumulating type dispersion thermal oxidation treatment device |
-
2020
- 2020-09-28 CN CN202022169529.XU patent/CN213746781U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114427687A (en) * | 2022-03-02 | 2022-05-03 | 山西亚乐士环保技术股份有限公司 | High-temperature low-oxygen heat accumulating type dispersion thermal oxidation treatment device |
| CN114427687B (en) * | 2022-03-02 | 2024-04-26 | 山西亚乐士环保技术股份有限公司 | High-temperature low-oxygen heat accumulating type heat dissipation oxidation treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110425550B (en) | Purifying and treating device and process for tar tail gas and asphalt smoke | |
| CN205909311U (en) | Heat accumulating type oxidation furnace | |
| CN210035535U (en) | Heat accumulating type thermal combustion furnace system | |
| CN108036665A (en) | Carbon baking furnace flue gas pollutant thermal accumulating incinerator and its processing method | |
| CN206269150U (en) | A kind of emission-control equipment based on RTO | |
| CN213746781U (en) | Three-chamber RTO exchange heat accumulation type waste gas incineration device | |
| CN102519049A (en) | Low energy consumption system for purifying and incinerating harmful gases | |
| CN111609415A (en) | Self-cleaning heat accumulating type thermal incineration device | |
| CN206803190U (en) | Waste gas burning stove and waste gas burning equipment | |
| CN206771385U (en) | A kind of heat storage burner for making fuel using organic exhaust gas | |
| CN210979883U (en) | Two-chamber high-efficiency heat-storage combustion device | |
| CN210861131U (en) | A purification and treatment device for tar tail gas and asphalt smoke | |
| CN211822441U (en) | RTO heat accumulation formula incinerator | |
| CN208687747U (en) | A kind of three Room RTO devices administered for industrial organic exhaust gas | |
| CN101122443B (en) | Environment-friendly type energy-saving electrode roasting furnace and its baked asphalt smoke processing method | |
| CN218154256U (en) | High-temperature type regenerative incinerator | |
| CN206669761U (en) | Heat accumulating type oxidative system | |
| CN215982553U (en) | Heat accumulating type incineration device | |
| CN206563304U (en) | A kind of heat accumulating type incineration device with cleaning function | |
| CN216010874U (en) | Catalytic combustion treatment device for organic waste gas | |
| CN211847828U (en) | System for treating tail gas containing acetylene carbide slag in process of producing acetylene by calcium carbide dry method | |
| CN107497261A (en) | Sodium hydrosulfite production low-temp methanol washes the high-temperature oxidation device of waste gas | |
| CN207378845U (en) | A kind of heat accumulating type VOC emission-control equipments | |
| CN205505032U (en) | Heat accumulating type catalytic oxidation device | |
| CN206540306U (en) | Highly effective energy-conserving environmental-protecting type gas furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |