CN219264311U - Organic waste gas burns treatment facility - Google Patents

Organic waste gas burns treatment facility Download PDF

Info

Publication number
CN219264311U
CN219264311U CN202320853051.3U CN202320853051U CN219264311U CN 219264311 U CN219264311 U CN 219264311U CN 202320853051 U CN202320853051 U CN 202320853051U CN 219264311 U CN219264311 U CN 219264311U
Authority
CN
China
Prior art keywords
component
waste gas
seat
purification
organic waste
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
Application number
CN202320853051.3U
Other languages
Chinese (zh)
Inventor
谢腊平
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anhui Yiqing Environmental Protection Engineering Co ltd
Original Assignee
Anhui Yiqing Environmental Protection Engineering Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Anhui Yiqing Environmental Protection Engineering Co ltd filed Critical Anhui Yiqing Environmental Protection Engineering Co ltd
Priority to CN202320853051.3U priority Critical patent/CN219264311U/en
Application granted granted Critical
Publication of CN219264311U publication Critical patent/CN219264311U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Abstract

The utility model provides organic waste gas incineration treatment equipment, which relates to the technical field of organic waste gas treatment and comprises a base component and a purification component, wherein an incineration component assembled by bolts is arranged above one end of the base component, a heat exchange component connected in a sleeved mode is arranged on the outer side of the upper part of the incineration component, a flow regulating component sleeved by bolts is arranged above the heat exchange component, a purification component sleeved by bolts is arranged below one end of the flow regulating component, and the purification component comprises a purification cabin and an inner support; the utility model mainly utilizes the upper arc coaming plate arranged on the outer side of the gas distributing seat, so that the waste gas flame sprayed by the nozzle can be concentrated to heat the fin group and the serpentine pipeline, and the pipeline chamber of the heat exchange assembly is independent of the heating cabin, so that the heated heat can be transferred to the outside through the absorbed water body to achieve the heat exchange effect, the effect of collecting and utilizing the waste gas heat is achieved, and the reutilization of waste heat is ensured.

Description

Organic waste gas burns treatment facility
Technical Field
The utility model relates to the technical field of organic waste gas treatment, in particular to organic waste gas incineration treatment equipment.
Background
The incinerator is a mature and stable organic waste gas treatment device at present, the regenerative incinerator can treat volatile organic gases and odor discharged in industrial production, the RTO system utilizes high-temperature oxidation to remove waste gas, the waste gas is converted into carbon dioxide and water vapor by controlling temperature, residence time, turbulence coefficient and oxygen amount, and heat released during waste gas decomposition is recovered.
When the existing waste gas incineration treatment equipment is used, generally, after waste gas is combusted, heat is absorbed, and then pollutants are removed and then discharged, for example, a heat accumulating type thermal plasma incineration device provided by application number CN202110243303.6 comprises: the bottom of the incinerator is communicated with a flue gas channel, and a plurality of thermal plasma torches are arranged at the top of the incinerator; the flue gas channel and the incinerator are internally paved with a plurality of heat storage heat exchangers which are mutually connected in series, and organic waste gas enters from one end of the heat storage heat exchangers which are mutually connected in series and is discharged from one end of the heat storage heat exchanger positioned in the incinerator to enter the incinerator through continuous heat storage; however, in the above-mentioned technologies, the heat of the exhaust gas is returned to the apparatus through the circulation pipe, and it is difficult to efficiently use the heat of the exhaust gas, so the present utility model proposes an organic exhaust gas incineration treatment apparatus to solve the problems existing in the prior art.
Disclosure of Invention
According to the organic waste gas incineration treatment equipment, the arc-shaped coaming is arranged on the outer side of the gas distribution seat, so that waste gas flames sprayed by the nozzles can be concentrated to heat the fin groups and the serpentine pipelines, and the pipeline chambers of the heat exchange assembly are independent of the heating cabin, so that heated heat can be transferred to the outside through the absorbed water body to achieve the heat exchange effect, the effect of collecting and utilizing waste gas heat is achieved, and the reutilization of waste heat is ensured.
In order to achieve the purpose of the utility model, the utility model is realized by the following technical scheme: the organic waste gas incineration treatment equipment comprises a base component and a purification component, wherein an incineration component assembled by bolts is arranged above one end of the base component, a heat exchange component connected in a sleeved mode is arranged on the outer side of the upper part of the incineration component, a flow regulation component sleeved by bolts is arranged above the heat exchange component, and a purification component sleeved by bolts is arranged below one end of the flow regulation component;
the purification assembly comprises a purification cabin, an inner support, a filter cotton layer, an extension duct, an adsorption layer, a humidifying block and an exhaust port, wherein the purification cabin is arranged below one end of the flow regulating assembly, the inner support is arranged inside the purification cabin, the filter cotton layer is arranged at the top of the inner support, the extension duct is arranged below the filter cotton layer, the adsorption layer is arranged below the extension duct, the humidifying block is arranged below the adsorption layer, and the exhaust port is connected with the output end of the purification cabin.
As a preferred embodiment of the present utility model, the filter cotton layer and the extension duct and the adsorption layer and the humidifying block are in a multi-layer parallel distribution structure, and the extension duct is in a non-straight duct structure.
As a preferred implementation mode of the utility model, the base component comprises a cushion block, a base plate, an assembly disc and a partition plate, the top side of the cushion block is provided with the base plate for installing the partition plate, the assembly disc assembled by bolts is arranged above two sides of the base plate, the incineration component comprises a sleeve seat, an air pump, an air inlet valve, an air inlet, an inner pipe, a compression block, an air dividing seat, an arc coaming, a nozzle and an electric shock head, the sleeve seat is arranged above a group of assembly discs, one end of the sleeve seat is provided with the air pump connected with the output end of the air inlet valve, and one end of the air inlet valve is provided with the air inlet.
As a preferred implementation mode of the utility model, an inner pipe for installing the compression block is arranged in the sleeve joint seat, a gas distribution seat is arranged above the inner pipe, an arc coaming is arranged at the edge of the gas distribution seat, nozzles distributed in an annular array are arranged above the gas distribution seat, and an electric shock head is arranged on the top edge side of the gas distribution seat.
As a preferred embodiment of the utility model, the heat exchange assembly comprises a heating cabin, a heat insulation board, a water inlet pipe, a water diversion seat, a coiled pipe, a water outlet pipe, a fin group and a sieve plate, wherein the heating cabin is arranged on the outer side of the arc-shaped coaming, the heat insulation board is arranged on the outer side of the heating cabin, the water inlet pipe is arranged at one end of the heat insulation board, the water diversion seat is arranged in the heating cabin, the coiled pipe is arranged at the inner end of the water diversion seat, the water outlet pipe is connected with the output end of the coiled pipe, the sleeved fin group is arranged on the outer side of the coiled pipe, and the sieve plate is arranged below the fin group.
As a preferred embodiment of the present utility model, the flow regulating assembly includes a top cover, a valve block, a cylinder, a valve core and a mechanical valve, wherein the top cover is disposed on the top side of the heating cabin, the valve block for mounting the cylinder is disposed on the top side of the top cover, the output end of the cylinder penetrates through the valve block to be connected with the valve core, and the output end of the valve block is connected with the mechanical valve.
The beneficial effects of the utility model are as follows:
the utility model mainly utilizes the upper arc coaming plate arranged on the outer side of the gas distributing seat, so that the waste gas flame sprayed by the nozzle can be concentrated to heat the fin group and the serpentine pipeline, and the pipeline chamber of the heat exchange assembly is independent of the heating cabin, so that the heated heat can be transferred to the outside through the absorbed water body to achieve the heat exchange effect, the effect of collecting and utilizing the waste gas heat is achieved, and the reutilization of waste heat is ensured.
Drawings
FIG. 1 is a schematic perspective view of the present utility model;
FIG. 2 is a schematic side view of the present utility model;
FIG. 3 is a schematic view of the heat exchange assembly and incineration components of the present utility model;
FIG. 4 is a schematic view of the purification assembly of the present utility model.
Wherein: 1. a base assembly; 101. a cushion block; 102. a base plate; 103. a mounting plate; 104. a partition plate; 2. an incineration member; 201. a socket is sleeved; 202. an air pump; 203. an intake valve; 204. an air inlet; 205. an inner tube; 206. a compression block; 207. an air dividing seat; 208. arc coaming; 209. a nozzle; 2010. an electric shock head; 3. a heat exchange assembly; 301. a heating chamber; 302. a heat insulating plate; 303. a water inlet pipe; 304. a water diversion seat; 305. a serpentine tube; 306. a water outlet pipe; 307. a fin group; 308. a sieve plate; 4. a flow regulating component; 401. a top cover; 402. a valve block; 403. a cylinder; 404. a valve core; 405. a mechanical valve; 5. a purification assembly; 501. a purification cabin; 502. an inner support; 503. a cotton filter layer; 504. extending the duct; 505. an adsorption layer; 506. a humidifying block; 507. and (5) discharging.
Detailed Description
The present utility model will be further described in detail with reference to the following examples, which are only for the purpose of illustrating the utility model and are not to be construed as limiting the scope of the utility model.
According to fig. 1-4, the embodiment provides an organic waste gas incineration treatment device, which comprises a base component 1 and a purification component 5, wherein an incineration component 2 assembled by bolts is arranged above one end of the base component 1, a heat exchange component 3 in sleeved connection is arranged on the outer side above the incineration component 2, a flow regulating component 4 in sleeved connection by bolts is arranged above the heat exchange component 3, and a purification component 5 in sleeved connection by bolts is arranged below one end of the flow regulating component 4;
the purification assembly 5 comprises a purification cabin 501, an inner support 502, a filter cotton layer 503, an extension duct 504, an adsorption layer 505, a humidifying block 506 and an exhaust port 507, wherein the purification cabin 501 is arranged below one end of the flow regulating assembly 4, the inner support 502 is arranged inside the purification cabin 501, the filter cotton layer 503 is arranged at the top of the inner support 502, the extension duct 504 is arranged below the filter cotton layer 503, the adsorption layer 505 is arranged below the extension duct 504, the humidifying block 506 is arranged below the adsorption layer 505, and the exhaust port 507 is connected with the output end of the purification cabin 501.
The filter cotton layer 503, the extension duct 504, the adsorption layer 505 and the humidifying block 506 are in a multi-layer parallel distribution structure, and the extension duct 504 is in a non-straight duct-shaped structure.
In this embodiment, the exhaust gas enters the purification chamber 501, is separated by the filter cotton layer 503, is physically contaminated, is retained for a long time by the extension duct 504, is adsorbed with a lot of contaminants by the adsorption layer 505, is humidified and removed by the humidifying block 506 after the adsorption is completed, and is discharged from the apparatus through the outlet 507 at the output end of the purification chamber 501 to complete the treatment.
The base component 1 comprises a cushion block 101, a base plate 102, an assembly disc 103 and a partition plate 104, the base plate 102 for installing the partition plate 104 is arranged on the top side of the cushion block 101, the assembly disc 103 assembled by bolts is arranged above two sides of the base plate 102, the incineration component 2 comprises a sleeve seat 201, an air pump 202, an air inlet valve 203, an air inlet 204, an inner pipe 205, a compression block 206, an air distribution seat 207, an arc-shaped coaming 208, a nozzle 209 and an electric shock head 2010, the sleeve seat 201 is arranged above one group of the assembly discs 103, an air pump 202 connected with the output end of the air inlet valve 203 is arranged at one end of the sleeve seat 201, and an air inlet 204 is arranged at one end of the air inlet valve 203.
In this embodiment, the air inlet valve 203 is opened, and the air pump 202 is started to output power to drive the output end of the air pump 202 to operate, so that the organic waste gas enters the air inlet valve 203 through the air inlet 204 and is then input into the socket 201 through the air pump 202.
The inside of the sleeve seat 201 is provided with an inner pipe 205 for installing a compression block 206, a gas distributing seat 207 is arranged above the inner pipe 205, the edge of the gas distributing seat 207 is provided with an arc-shaped coaming 208, nozzles 209 distributed in an annular array are arranged above the gas distributing seat 207, and the top edge side of the gas distributing seat 207 is provided with an electric shock head 2010.
In this embodiment, the flow rate of the organic waste gas can be accelerated by the compression block 206 in the inner pipe 205, the heated area of combustion is increased, and finally the organic waste gas is sprayed out by the nozzle 209 on the top side of the gas separation seat 207, and the organic waste gas is ignited by the high Wen Dianji generated by the electric shock head 2010, so that the heat of combustion can be guided upwards by the upper arc-shaped surrounding plate 208.
The heat exchange assembly 3 comprises a heating cabin 301, a heat insulation plate 302, a water inlet pipe 303, a water diversion seat 304, a coiled pipe 305, a water outlet pipe 306, a fin group 307 and a sieve plate 308, wherein the heating cabin 301 is arranged on the outer side of the arc-shaped enclosing plate 208, the heat insulation plate 302 is arranged on the outer side of the heating cabin 301, the water inlet pipe 303 is arranged at one end of the heat insulation plate 302, the water diversion seat 304 is arranged in the heating cabin 301, the coiled pipe 305 is arranged at the inner end of the water diversion seat 304, the water outlet pipe 306 is connected with the output end of the coiled pipe 305, the sleeved fin group 307 is arranged on the outer side of the coiled pipe 305, and the sieve plate 308 is arranged below the fin group 307.
In this embodiment, after the incineration component 2 is combusted, water is input through the water inlet pipe 303 and is emitted to the coiled pipe 305 through the water diversion seat 304, so that the coiled pipe 305 and the fin group 307 absorb heat of flame and then are conducted into the water in the coiled pipe 305, and the heated water is output to a target place through the water outlet pipe 306, so that the heat exchange effect is achieved.
The flow regulating assembly 4 comprises a top cover 401, a valve block 402, an air cylinder 403, a valve core 404 and a mechanical valve 405, wherein the top cover 401 is arranged on the top side of the heating cabin 301, the valve block 402 for installing the air cylinder 403 is arranged on the top side of the top cover 401, the valve core 404 is connected with the output end of the air cylinder 403 penetrating through the valve block 402, and the mechanical valve 405 is connected with the output end of the valve block 402.
In this embodiment, the burned exhaust gas is input to the top cover 401 through the heating chamber 301, the mechanical valve 405 is opened, and the actuating cylinder 403 outputs power to drive the output end of the cylinder 403 to operate, so that the output end of the cylinder 403 drives the valve core 404 to open the valve block 402, and through opening the valve block 402, the organic exhaust gas is input into the purifying assembly 5 through the flow regulating assembly 4.
The working principle of the organic waste gas incineration treatment equipment is as follows: through opening admission valve 203 to start air pump 202 output power drives air pump 202 output and carries out the operation, make organic waste gas enter into admission valve 203 through air inlet 204, the inside of cup jointing seat 201 is input to the rethread air pump 202, through the compression piece 206 among the inner tube 205, can let organic waste gas carry out the velocity of flow and accelerate, increase the heated area of burning, finally spray out through the nozzle 209 of gas separation seat 207 topside, produce high Wen Dianji through electric shock head 2010 and ignite organic waste gas, the heat water conservancy diversion that can be with the burning upwards in the cooperation of arc bounding wall 208, after incineration part 2 is through burning, input water through inlet tube 303, distribute to on the serpentine 305 through water diversion seat 304, in this serpentine 305 and fin group 307 are with the heat absorption back of flame, the water among the serpentine 305, the water after the heating is exported to the target place through outlet pipe 306, so as to reach the effect of heat transfer, the waste gas after the burning is input to top cap 401 through heating cabin 301, open mechanical valve 405, and start cylinder 403 output power drives cylinder 403 output and carries out the operation, so cylinder 403 output drives valve core 404 and makes valve block 402, make valve block 402 open, through valve block 402, through opening 506 through the valve block 402, remove impurity and remove the time through the humidification layer through the stack of adjusting and the humidity control device, remove impurity and remove the filter element through the filter element 506, remove impurity and remove the impurity through the filter element, remove impurity and remove the impurity through the filter element through the absorption layer of the filter element, and remove impurity through the filter element, remove impurity through the filter element.
The foregoing has shown and described the basic principles, principal features and advantages of the utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.

Claims (6)

1. An organic waste gas incineration treatment device, comprising a base component (1) and a purification component (5), characterized in that: an incineration component (2) assembled by bolts is arranged above one end of the base component (1), a heat exchange component (3) which is connected in a sleeved mode is arranged on the outer side of the upper portion of the incineration component (2), a flow regulating component (4) sleeved by bolts is arranged above the heat exchange component (3), and a purification component (5) sleeved by bolts is arranged below one end of the flow regulating component (4);
the purification assembly (5) comprises a purification cabin (501), an inner support (502), a filter cotton layer (503), an extension duct (504), an adsorption layer (505), a humidifying block (506) and a discharge port (507), wherein the purification cabin (501) is arranged below one end of the flow regulating assembly (4), the inner support (502) is arranged inside the purification cabin (501), the filter cotton layer (503) is arranged at the top of the inner support (502), the extension duct (504) is arranged below the filter cotton layer (503), the adsorption layer (505) is arranged below the extension duct (504), the humidifying block (506) is arranged below the adsorption layer (505), and the discharge port (507) is connected to the output end of the purification cabin (501).
2. An organic waste gas incineration disposal apparatus according to claim 1, characterised in that: the filter cotton layer (503) and the extension duct (504) and the adsorption layer (505) and the humidifying block (506) are in a multi-layer parallel distribution structure, and the extension duct (504) is in a non-straight duct-shaped structure.
3. An organic waste gas incineration disposal apparatus according to claim 1, characterised in that: the base assembly (1) comprises a cushion block (101), a base plate (102), an assembly plate (103) and a partition plate (104), the base plate (102) for installing the partition plate (104) is arranged on the top side of the cushion block (101), the assembly plate (103) assembled by bolts is arranged on the upper sides of two sides of the base plate (102), the incineration component (2) comprises a sleeve seat (201), an air pump (202), an air inlet valve (203), an air inlet (204), an inner pipe (205), a compression block (206), an air distribution seat (207), an arc-shaped coaming (208), a nozzle (209) and an electric shock head (2010), the sleeve seat (201) is arranged above the assembly plate (103), one end of the sleeve seat (201) is provided with the air pump (202) connected with the output end of the air inlet valve (203), and one end of the air inlet valve (203) is provided with the air inlet (204).
4. An organic waste gas incineration disposal apparatus according to claim 3, characterised in that: the inside of cup jointing seat (201) is provided with inner tube (205) of installation compression piece (206), the top of inner tube (205) is provided with divides gas seat (207), just the edge of dividing gas seat (207) is provided with arc bounding wall (208), the top of dividing gas seat (207) is provided with nozzle (209) that annular array distributes, the topside of dividing gas seat (207) is provided with electric shock head (2010).
5. An organic waste gas incineration disposal apparatus according to claim 4, characterised in that: the heat exchange assembly (3) comprises a heating cabin (301), a heat insulation board (302), a water inlet pipe (303), a water diversion seat (304), a coiled pipe (305), a water outlet pipe (306), a fin group (307) and a sieve plate (308), wherein the heating cabin (301) is arranged on the outer side of the arc-shaped coaming (208), the heat insulation board (302) is arranged on the outer side of the heating cabin (301), the water inlet pipe (303) is arranged at one end of the heat insulation board (302), the water diversion seat (304) is arranged in the heating cabin (301), the coiled pipe (305) is arranged at the inner end of the water diversion seat (304), the water outlet pipe (306) is connected with the output end of the coiled pipe (305), the sleeved fin group (307) is arranged on the outer side of the coiled pipe (305), and the sieve plate (308) is arranged below the fin group (307).
6. An organic waste gas incineration disposal apparatus according to claim 5, characterised in that: the flow regulating assembly (4) comprises a top cover (401), a valve block (402), an air cylinder (403), a valve core (404) and a mechanical valve (405), wherein the top cover (401) is arranged on the top side of the heating cabin (301), the valve block (402) for installing the air cylinder (403) is arranged on the top side of the top cover (401), the output end of the air cylinder (403) penetrates through the valve block (402) to be connected with the valve core (404), and the output end of the valve block (402) is connected with the mechanical valve (405).
CN202320853051.3U 2023-04-17 2023-04-17 Organic waste gas burns treatment facility Active CN219264311U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202320853051.3U CN219264311U (en) 2023-04-17 2023-04-17 Organic waste gas burns treatment facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202320853051.3U CN219264311U (en) 2023-04-17 2023-04-17 Organic waste gas burns treatment facility

Publications (1)

Publication Number Publication Date
CN219264311U true CN219264311U (en) 2023-06-27

Family

ID=86859673

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202320853051.3U Active CN219264311U (en) 2023-04-17 2023-04-17 Organic waste gas burns treatment facility

Country Status (1)

Country Link
CN (1) CN219264311U (en)

Similar Documents

Publication Publication Date Title
CN110585855A (en) Movable waste gas treatment device
CN212962199U (en) Vertical boiler
CN201628227U (en) Remains and offering incineration and post-treatment equipment
CN101352639B (en) Organic waste gas treatment system
CN105003924B (en) Swinging RTO combustion systems
CN219264311U (en) Organic waste gas burns treatment facility
CN111780135A (en) Low-pollution type RTO combustion furnace
CN214552358U (en) Double-rotary-wheel high-concentration organic waste gas treatment system
CN214223130U (en) VOC high-efficiency treatment equipment
CN209840118U (en) Energy-conserving RTO heat accumulation formula burns burning furnace
CN216558415U (en) Waste gas treatment system is scribbled to coloured silk
CN217584480U (en) Energy-saving waste gas incinerator
CN214791179U (en) Tail gas treatment and waste heat recovery device
CN108151037A (en) A kind of complicated organic exhaust gas low-temperature heat accumulating catalytic combustion process method of removing
CN212157197U (en) Handle heat accumulation formula heating power incinerator for VOC
CN219607088U (en) Funeral and interment incinerator using oxyhydrogen energy
CN217795369U (en) Organic waste gas pollution-reducing carbon-reducing treatment equipment
CN216047748U (en) Heat accumulating type oxidation incinerator
CN215259863U (en) TO incinerator
CN215085993U (en) Double-rotating-wheel high-efficiency organic waste gas treatment system
CN219083117U (en) VOC incinerator
CN211739152U (en) Adjustable multi-return-stroke dust removal integrated device for high-temperature air preheater
CN211399828U (en) RCO organic waste gas adsorption desorption catalytic combustion integration equipment
CN220802559U (en) Paint mist waste gas treatment device
CN210495805U (en) High-efficiency volatile organic waste gas treatment system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant