CN211667832U - Heat accumulating type oxidation furnace - Google Patents
Heat accumulating type oxidation furnace Download PDFInfo
- Publication number
- CN211667832U CN211667832U CN201922470076.1U CN201922470076U CN211667832U CN 211667832 U CN211667832 U CN 211667832U CN 201922470076 U CN201922470076 U CN 201922470076U CN 211667832 U CN211667832 U CN 211667832U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- fixedly connected
- fresh air
- oxidation
- heat storage
- 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
Images
Abstract
The utility model discloses a heat accumulating type oxidation furnace, including the main furnace body, its characterized in that: the utility model relates to a flue gas cracking technique field, including the main furnace body, the oxidation chamber lower part evenly is equipped with three ceramic regenerator, the pipeline fixedly connected with waste gas pipeline is passed through in the leftmost side of ceramic regenerator below, and middle pipeline fixedly connected with fresh air pipeline, pipeline fixedly connected with fresh air discharge pipeline are passed through in the rightmost side, all be connected with the change-over valve between fresh air pipeline and each ceramic regenerator, fresh air discharge pipeline pass through pipeline fixedly connected with and discharge the chimney, and all be connected with the change-over valve between each ceramic regenerator, the oxidation chamber top end fixedly connected with flame jet mouth, the utility model relates to a flue gas cracking technique field. This heat accumulation formula oxidation furnace has reached high-efficient redox, the operation of being convenient for, and temperature control is accurate, and gas emission is up to standard purpose, and equipment security has very big promotion.
Description
Technical Field
The utility model relates to a waste gas cracking technical field specifically is a heat accumulation formula oxidation furnace.
Background
The natural resources are continuously reduced while the world population is continuously increased, globalization and the pursuit of economic prosperity of human beings are realized, the common prosperity and development can be realized only by effectively reducing the resource consumption and avoiding emission, the organic matters in the process waste gas generated in the industry are burnt at high temperature and are converted into water and carbon dioxide, the air purification process which is most effective for treating combustible organic pollutants is provided, the regenerative thermal oxidation furnace is generally used for cleaning combustible pollutant components which can generate peculiar smell, the regenerative thermal oxidation furnace is widely applied to the industries of chemical industry, medicine, printing, food and the like due to the higher internal heat recovery capacity of the regenerative thermal oxidation furnace, the principle is to oxidize the organic matters in the waste gas into corresponding carbon dioxide and water at high temperature so as to purify the waste gas and recover the heat released when the waste gas is decomposed, the waste gas decomposition efficiency of the three-chamber oxidation furnace reaches more than 99 percent, the heat recovery efficiency reaches more than 95 percent. The main structure of the oxidation furnace consists of an oxidation chamber, a heat storage chamber, a switching valve and the like. According to the actual demand of a customer, different heat energy recovery modes and switching valve modes are selected, but in the prior art, the problems of incomplete oxidation, overlarge equipment volume, high cost, difficult operation and the like exist. This heat accumulation formula oxidation furnace through being equipped with ceramic heat accumulator, fine recycles the heat, has reduced oxidation furnace heating cost, and the oxidation is thorough, convenient operation.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
The utility model provides a not enough to prior art, the utility model provides a regenerative oxidation furnace has solved the oxidation of existing equipment thoroughly, and equipment volume is too big, removes and operates inconveniently, and the problem of a large amount of wastes of heat.
(II) technical scheme
1. In order to achieve the above purpose, the utility model discloses a following technical scheme realizes: a regenerative oxidation furnace comprises a main furnace body, and is characterized in that: the utility model discloses a blast furnace, including main furnace body, oxidation chamber, pipeline fixedly connected with waste gas pipeline, pipeline fixedly connected with fresh air pipeline, pipeline fixedly connected with fresh air discharge pipeline, the main furnace body upper portion is equipped with the oxidation chamber, the oxidation chamber lower part evenly is equipped with three ceramic regenerator, pipeline fixedly connected with waste gas pipeline is passed through to ceramic regenerator below leftmost side, and the centre is through pipeline fixedly connected with fresh air pipeline, and pipeline fixedly connected with fresh air discharge pipeline passes through the pipeline fixedly connected with discharge chimney, and all be connected with the change-over valve between each ceramic regenerator, oxidation chamber top.
The ceramic heat storage chambers comprise a first ceramic heat storage chamber, a second ceramic heat storage chamber and a third ceramic heat storage chamber.
Preferably, a thermometer is fixedly connected between the main furnace body and the oxidation chamber.
Preferably, the left end pipeline of the fresh air pipeline is fixedly connected with an air blower.
Preferably, the exhaust chimney is provided with a filter layer at the lower end of the exhaust port.
Preferably, the main furnace body is fixedly connected with a heat-preservation, heat-insulation and explosion-proof layer outside.
Preferably, the left side and the right side of the heat-preservation, heat-insulation and explosion-proof layer are respectively provided with a hanging ring.
(III) advantageous effects
The regenerative oxidation furnace. The method has the following beneficial effects:
(1) this heat accumulation formula oxidation furnace is equipped with three ceramic regenerator in the oxidizing chamber, can realize high-efficient oxidation, and the oxidation is more thorough, and the heat obtains high reusability, and operates and discharges the convenience.
(2) This heat accumulation formula oxidation furnace, oxidizing chamber, ceramic regenerator and pipeline directly link to each other, have reduced the equipment volume for the workman operates more conveniently, discharges more high-efficiently, has improved work efficiency greatly.
(3) This heat accumulation formula oxidation furnace, the top is equipped with the thermometer, can know the indoor temperature of oxidation in real time, reaches the purpose to the accurate control of oxidation temperature.
(4) This heat accumulation formula oxidation furnace, chimney discharge port lower extreme are equipped with the filter layer, discharge last step, filter, can make the effective discharge to reach standard of exhaust gas discharge.
Drawings
FIG. 1 is a schematic structural view of the utility model;
FIG. 2 is a schematic diagram of a ceramic regenerator.
In the figure: the device comprises a main furnace body 1, an oxidation chamber 2, a ceramic regenerator 3, a waste gas pipeline 4, a blower 5, a fresh air pipeline 6, a fresh air discharge pipeline 7, a change-over valve 8, a filter layer 9, a discharge chimney 10, a flame nozzle 11, a thermometer 12, a heat-preservation, heat-insulation and explosion-proof layer 13 and a hanging ring 14.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, the present invention provides a technical solution: the utility model provides a regenerative oxidation furnace, includes main furnace body 1, 1 upper portion of main furnace body is equipped with oxidation chamber 2, 2 lower parts in oxidation chamber evenly are equipped with three ceramic regenerator 3, 3 below leftmost sides in ceramic regenerator are through pipeline fixedly connected with exhaust duct 4, and the centre is through pipeline fixedly connected with fresh air pipeline 6, and the rightmost side is through pipeline fixedly connected with fresh air discharge pipeline 7, all be connected with change-over valve 8 between fresh air pipeline 6 and each ceramic regenerator 3, fresh air discharge pipeline 7 discharges chimney 10 through pipeline fixedly connected with, and all be connected with change-over valve 8 with each ceramic regenerator 3 within a definite time, 2 top fixedly connected with flame jet nozzle 11 in oxidation chamber.
The ceramic regenerator 3 includes a first ceramic regenerator 31, a second ceramic regenerator 32, and a third ceramic regenerator 33.
During the use, waste gas is let in to waste gas pipeline 4, first ceramic regenerator 31, second ceramic regenerator 32, third ceramic regenerator 33 is heat accumulation in turn, it is exothermic, when first ceramic regenerator 31 is exothermic, the second, third ceramic regenerator carries out the heat accumulation, first ceramic regenerator 31 new air pipeline 6 change-over valve 8 is opened, new air discharge pipeline 7 change-over valve is closed, otherwise the same, cycle work, the thermometer can real-time detection oxidation chamber 2 internal temperature, if need remove, then the removal of equipment is carried out to the accessible rings.
It is noted that, herein, relational terms such as first and second, and the like may be 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. Also, 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. Without further limitation. The use of the phrase "comprising one of the elements does not exclude the presence of other like elements in the process, method, article, or apparatus that comprises the element.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. A regenerative oxidation furnace comprises a main furnace body (1), and is characterized in that: the furnace is characterized in that an oxidation chamber (2) is arranged on the upper part of the main furnace body (1), three ceramic heat storage chambers (3) are uniformly arranged on the lower part of the oxidation chamber (2), a waste gas pipeline (4) is fixedly connected to the leftmost side of the lower part of each ceramic heat storage chamber (3) through a pipeline, a fresh air pipeline (6) is fixedly connected to the middle of the lower part of each ceramic heat storage chamber through a pipeline, a fresh air discharge pipeline (7) is fixedly connected to the rightmost side of the lower part of each ceramic heat storage chamber through a pipeline, a change-over valve (8) is connected between each fresh air pipeline (6) and each ceramic heat storage chamber (3), a discharge chimney (10) is fixedly connected to each fresh air discharge pipeline (7) through a pipeline, a change-over valve (8) is;
the ceramic heat storage chamber (3) comprises a first ceramic heat storage chamber (31), a second ceramic heat storage chamber (32) and a third ceramic heat storage chamber (33).
2. A regenerative thermal oxidizer as set forth in claim 1, wherein: a thermometer (12) is fixedly connected between the main furnace body (1) and the oxidation chamber (2).
3. A regenerative thermal oxidizer as set forth in claim 1, wherein: and the left end pipeline of the fresh air pipeline (6) is fixedly connected with an air blower (5).
4. A regenerative thermal oxidizer as set forth in claim 1, wherein: and a filter layer (9) is arranged at the lower end of the discharge outlet of the discharge chimney (10).
5. A regenerative thermal oxidizer as set forth in claim 1, wherein: the main furnace body (1) is fixedly connected with a heat-preservation, heat-insulation and explosion-proof layer (13) outside.
6. A regenerative thermal oxidizer as set forth in claim 5, wherein: the left side and the right side of the heat-preservation, heat-insulation and explosion-proof layer (13) are respectively provided with a hanging ring (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922470076.1U CN211667832U (en) | 2019-12-31 | 2019-12-31 | Heat accumulating type oxidation furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922470076.1U CN211667832U (en) | 2019-12-31 | 2019-12-31 | Heat accumulating type oxidation furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211667832U true CN211667832U (en) | 2020-10-13 |
Family
ID=72736138
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922470076.1U Active CN211667832U (en) | 2019-12-31 | 2019-12-31 | Heat accumulating type oxidation furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211667832U (en) |
-
2019
- 2019-12-31 CN CN201922470076.1U patent/CN211667832U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205659976U (en) | Fusion method industry sodium chloride abraum salt treatment facility | |
| CN210398945U (en) | Emission reduction system for gravure organic waste gas | |
| CN101352639B (en) | Organic waste gas treatment system | |
| CN211667832U (en) | Heat accumulating type oxidation furnace | |
| CN206514309U (en) | A kind of coating waste gas processing unit | |
| CN209362216U (en) | A kind of refractory material exhaust gas comprehensive treatment system | |
| CN208253609U (en) | A kind of printing machine VOCs concentration paddy electricity balance RTO processing system | |
| CN205505032U (en) | Heat accumulating type catalytic oxidation device | |
| CN209279177U (en) | A kind of heat accumulating type Catalytic oxidation furnace | |
| CN210241600U (en) | RCO heat accumulating type catalytic combustion device | |
| CN209893425U (en) | Industrial organic waste gas incinerator | |
| CN209639036U (en) | The novel VOCs disposal plant to be cooperated based on RTO and RCO | |
| CN209801505U (en) | RTO exhaust treatment device | |
| CN208011740U (en) | A kind of automatically cleaning regenerative thermal oxidizer | |
| CN209221872U (en) | A kind of recuperative heater flue gas denitrification system of two-stage accumulation of heat | |
| CN107036109A (en) | Sodium dithionite produces the processing system and processing method of waste gas | |
| CN202993238U (en) | Boiler flue heat recovery energy-saving and environment-friendly system | |
| CN207302754U (en) | A kind of horizontal environmentally friendly enamelling machine | |
| CN113324257A (en) | Heat collection type RTO treatment system suitable for high-concentration VOCs waste gas | |
| CN205939175U (en) | Organic gas burns device | |
| CN207035156U (en) | Modified RTO emission-control equipments | |
| CN206215040U (en) | VOCs processes reaction unit | |
| CN106540499A (en) | A kind of boiler smoke multiple stage filtration system | |
| CN213207882U (en) | Organic waste gas heat accumulation formula oxidation unit | |
| CN110433621A (en) | A kind of method and device thereof of kiln gas charcoal reduction denitration |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |