CN105674294B - A kind of solid-liquid-gas three phase product classification discharge refuse burner - Google Patents
A kind of solid-liquid-gas three phase product classification discharge refuse burner Download PDFInfo
- Publication number
- CN105674294B CN105674294B CN201610164162.8A CN201610164162A CN105674294B CN 105674294 B CN105674294 B CN 105674294B CN 201610164162 A CN201610164162 A CN 201610164162A CN 105674294 B CN105674294 B CN 105674294B
- Authority
- CN
- China
- Prior art keywords
- outlet
- furnace
- gas
- wall
- recyclegas
- 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
- 238000001816 cooling Methods 0.000 claims abstract description 48
- 239000002699 waste material Substances 0.000 claims abstract description 19
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 16
- 238000010304 firing Methods 0.000 claims abstract description 7
- 239000002893 slag Substances 0.000 claims abstract description 7
- 230000008676 import Effects 0.000 claims description 30
- 238000002485 combustion reaction Methods 0.000 claims description 10
- 239000010808 liquid waste Substances 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 6
- 239000002826 coolant Substances 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 6
- 239000007787 solid Substances 0.000 abstract description 4
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000000498 cooling water Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2900/00—Special features of, or arrangements for incinerators
- F23G2900/00001—Exhaust gas recirculation
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Classify the invention discloses a kind of solid-liquid-gas three phase product and refuse burner is discharged, house refuse is out of top filling furnace chamber, air is passed through from bottom in furnace chamber, so that rubbish burns bottom-up in furnace chamber, the moisture content that burning generates takes furnace body out of in the form of steam with recyclegas, recyclegas returns to furnace chamber after cooling removal condensed water outside furnace body and carries out second-time burning, the gas that burning generates passes through second-time burning, realize fully burning, final tail gas is discharged by offgas outlet, heat in tail gas is utilized by heat exchange, it is discharged by slag-drip opening in the solid slag that furnace cavity bottom burning generates, waste residue can be recycled by separation, to realize that the solid-liquid-gas three phase product classification processing that incineration firing generates utilizes, the environmental pollution in garbage processing procedure is reduced to the full extent.
Description
Technical field
The present invention relates to technical field of waste treatment more particularly to a kind of solid-liquid-gas three phase product classification discharge incineration firings
Stove.
Background technology
In recent years, with the improvement of people's living standards, Municipal Domestic Garbage Output grows at top speed, sanitary fill over the years
Storage is huge.The mode of generally use garbage loading embeading is handled, and rubbish is caused to corrode a large amount of soils.Burning method can be real to greatest extent
Existing house refuse is effectively treated, and land occupation resource is minimum, however such as unprocessed direct emission of incineration tail gas, can be right
Air pollution is serious.Therefore, how efficiently, low cost, contamination-freely to house refuse carry out more thoroughly cleaning, it has also become
Those skilled in the art's urgent problem to be solved.
Invention content
To solve technical problem present in background technology, the present invention proposes a kind of solid-liquid-gas three phase product classification discharge rubbish
Rubbish combustion furnace.
A kind of solid-liquid-gas three phase product classification discharge refuse burner proposed by the present invention, including：Combustion furnace, waste residue discharge
Device, exhaust gas processing device, liquid waste treating apparatus；
Furnace interior has the furnace chamber for incineration firing, and garbage inlet, the furnace cavity bottom are equipped at the top of the furnace chamber
Equipped with slag-drip opening, combustion furnace includes upper furnace body and lower furnace body；
Upper furnace body furnace wall includes wall and first time wall on first, and wall is set on first outside wall on second,
Wall has double-layer structure on first, is formed between the double-layer structure and recycles gas chamber, recycles gas chamber and is equipped with the
One import, first outlet, the second import, second outlet, the first import and second outlet are connected to furnace chamber, recycle in gas chamber
Equipped with cycle admission line, cycle admission line both ends are connected to the second import and second outlet respectively, and wall is by the on second
One tube body coiled coil forms, and the two adjacent rings pipeline section of the first tube body abuts against each other, the first tube body both ends be respectively equipped with third into
Mouthful and third outlet, form the first cooling cavity on first on wall and second between wall, the first cooling cavity is equipped with the
Four imports, the 4th outlet, by pipeline and the 4th outlet, described first cools down and is equipped in cavity exhaust gas processing device
Cooling pipe, cooling pipe are interior filled with cooling medium；
Lower furnace body furnace wall includes first time coaming plate and second time coaming plate, and second time coaming plate is set in outside first time coaming plate,
The second cooling cavity is formed between first time coaming plate and second time coaming plate, and cooling medium is filled in the second cooling cavity,
Lower furnace body furnace wall is equipped with air intake and offgas outlet, and the offgas outlet passes through pipeline and the 4th inlet communication；
Liquid waste treating apparatus includes cooler bin, circulating cooling pipe, waste collection slot, and circulating cooling pipe is arranged in cooler bin
Interior, circulating cooling pipe both ends are connect with the second import and first outlet respectively, and circulating cooling pipe is equipped with the 5th outlet, and waste liquid is received
Collect slot and the 5th outlet；
Waste residue discharger is arranged at the slag-drip opening, and waste residue discharger includes multiple deslagging units, each deslagging
Unit includes dregs discharge tube and screw feed mechanism, is had along the axially extending storage slag cavity of dregs discharge tube, dregs discharge tube inside dregs discharge tube
Top has the first opening and is connected to the furnace chamber by first opening, and dregs discharge tube end is equipped with discharge port, and spiral is sent
Material mechanism is located in dregs discharge tube and is axially arranged along dregs discharge tube.
Preferably, circulating cooling pipe includes recyclegas air inlet pipe and recyclegas muffler, and third is equipped in cooler bin
Cooling cavity, the third cooling cavity is equipped with the second opening and third opening, between second opening and third opening
Form the channel for accommodating recyclegas air inlet pipe, recyclegas air inlet pipe is arranged in the channel and both ends be each passed through it is described
Second opening and third opening, recyclegas air inlet pipe be equipped with the 6th import, the 6th outlet, the 5th outlet, the 6th import and
6th outlet is located at second opening far from cooler bin side, and the 6th import and second outlet be by piping connection, the
With the second import by piping connection, the 5th outlet is located at third opening far from cooler bin side, recyclegas return-air for six outlets
Pipe is located in recyclegas air inlet pipe, recyclegas muffler first end and the 6th outlet, recyclegas muffler second
End is equipped with the 4th opening being connected to recyclegas air inlet pipe.
Preferably, the 6th import is located at the 6th outlet top, and recyclegas air inlet pipe is vertically arranged, and the 5th outlet, which is located at, to be followed
Ring gas inlet bottom of the tube.
Preferably, recyclegas escape pipe and recyclegas air inlet pipe are coaxially disposed, recyclegas outlet bottom of the tube with follow
It is spaced a predetermined distance between 4th opening of ring gas inlet pipe.
Preferably, the third cooling cavity, the second cooling cavity, the first cooling cavity pass sequentially through pipeline
Connection.
Preferably, second outlet is equipped with recyclegas conduit, and recyclegas conduit is vertically arranged in the furnace chamber, follows
Ring gas conduit stretches into the furnace chamber lower part far from second outlet one end.
Preferably, recyclegas conduit is located at far from second outlet one end above offgas outlet.
In the present invention, the solid-liquid-gas three phase product classification discharge refuse burner proposed, house refuse is inserted from top
In furnace chamber, air is passed through from bottom in furnace chamber so that rubbish burns bottom-up in furnace chamber, and the moisture content for generation of burning is with steam
Form take furnace body out of with recyclegas, recyclegas outside furnace body through it is cooling remove condensed water after return to furnace chamber and carry out secondary combustion
It burns, the gas for generation of burning realizes fully burning, final tail gas is discharged by offgas outlet, in tail gas by second-time burning
Heat is utilized by heat exchange, is discharged by slag-drip opening in the solid slag that furnace cavity bottom burning generates, waste residue is by detaching energy
It enough recycles, to realize that the solid-liquid-gas three phase product classification processing that incineration firing generates utilizes, reduces rubbish to the full extent
Environmental pollution in rubbish processing procedure.
Description of the drawings
Fig. 1 is a kind of structural schematic diagram of solid-liquid-gas three phase product classification discharge refuse burner proposed by the present invention.
Specific implementation mode
As shown in FIG. 1, FIG. 1 is a kind of structures of solid-liquid-gas three phase product classification discharge refuse burner proposed by the present invention
Schematic diagram.
Referring to Fig.1, a kind of solid-liquid-gas three phase product classification discharge refuse burner proposed by the present invention, including：Combustion furnace,
Waste residue discharger, exhaust gas processing device 3, liquid waste treating apparatus；
Furnace interior has the furnace chamber for incineration firing, and garbage inlet, the furnace cavity bottom are equipped at the top of the furnace chamber
Equipped with slag-drip opening, combustion furnace includes upper furnace body 11 and lower furnace body 12；
11 furnace wall of upper furnace body includes wall and first time wall on first, and wall is set on first outside wall on second
Portion, wall has double-layer structure on first, is formed between the double-layer structure and recycles gas chamber, recycled gas chamber and be equipped with
First import, first outlet, the second import, second outlet, the first import and second outlet are connected to furnace chamber, recycle gas chamber
Interior to be equipped with cycle admission line 2,2 both ends of cycle admission line are connected to the second import and second outlet respectively, wall on second
It is formed by 4 coiled coil of the first tube body, the two adjacent rings pipeline section of the first tube body 4 abuts against each other, and 4 both ends of the first tube body are respectively equipped with
Third import and third export, and form the first cooling cavity on first on wall and second between wall, first cools down on cavity
Equipped with the 4th import, the 4th outlet, for exhaust gas processing device 3 by pipeline and the 4th outlet, first cooling is empty
Intracavitary is equipped with cooling pipe 5, and cooling medium is filled in cooling pipe 5；Second outlet is equipped with recyclegas conduit 8, cycle
Gas conduit 8 is vertically arranged in the furnace chamber, and recyclegas conduit 8 stretches into the furnace chamber lower part far from second outlet one end,
Recyclegas conduit 8 is located at far from second outlet one end above offgas outlet；
12 furnace wall of lower furnace body includes first time coaming plate and second time coaming plate, and second time coaming plate is set in outside first time coaming plate
Portion forms the second cooling cavity, is situated between filled with cooling in the second cooling cavity between first time coaming plate and second time coaming plate
Matter, 12 furnace wall of lower furnace body are equipped with air intake and offgas outlet, and the offgas outlet passes through pipeline and the 4th inlet communication；
Liquid waste treating apparatus includes cooler bin 61, circulating cooling pipe 62, waste collection slot, and circulating cooling pipe 62 is vertically arranged
In cooler bin 61,62 both ends of circulating cooling pipe are connect with the second import and first outlet respectively, and circulating cooling pipe 62 is equipped with
5th outlet, waste collection slot and the 5th outlet；In specific setting, circulating cooling pipe 62 include recyclegas air inlet pipe and
Recyclegas muffler is equipped with third in cooler bin 61 and cools down cavity, and the third cooling cavity is equipped with the second opening and the
Three openings form the channel for accommodating recyclegas air inlet pipe, recyclegas air inlet pipe between second opening and third opening
It is arranged in the channel and both ends are each passed through second opening and third opening, recyclegas air inlet pipe are equipped with the 6th
Import, the 6th outlet, the 5th outlet, the 6th import and the 6th outlet are located at second opening far from 61 side of cooler bin and the
Six imports are located at the 6th outlet top, and the 6th import passes through piping connection, the 6th outlet and the second import with second outlet
By piping connection, the 5th outlet is located at third opening far from 61 side of cooler bin, and recyclegas muffler is located at recyclegas
In air inlet pipe, recyclegas escape pipe is coaxially disposed with recyclegas air inlet pipe, recyclegas outlet bottom of the tube and recyclegas
It is spaced a predetermined distance between 4th opening of air inlet pipe, recyclegas muffler first end and the 6th outlet, recyclegas
Muffler second end is equipped with the 4th opening being connected to recyclegas air inlet pipe；
Waste residue discharger is arranged at the slag-drip opening, and waste residue discharger includes multiple deslagging units, each deslagging
Unit includes dregs discharge tube 71 and screw feed mechanism 72, and 71 inside of dregs discharge tube has empty along the axially extending storage slag of dregs discharge tube 71
Chamber, 71 top of dregs discharge tube have the first opening and are connected to the furnace chamber by first opening, and 71 end of dregs discharge tube is equipped with
Discharge port, screw feed mechanism 72 are located in dregs discharge tube 71 and along the axial settings of dregs discharge tube 71.
The present embodiment solid-liquid-gas three phase product classification discharge refuse burner specific work process in, house refuse from
Top insert furnace chamber in, air is passed through from bottom in furnace chamber so that rubbish burns bottom-up in furnace chamber, furnace chamber temperature by
It continuously decreases down, solid slag is discharged from furnace cavity bottom by deslagging outlet, so that combustion of the rubbish in furnace chamber upwards
It burns layer to be held in place, in combustion, the recyclegas in furnace chamber is discharged from top, after cooling removal vapor
Return to furnace chamber；The moisture content that burning generates takes furnace body out of in the form of steam with recyclegas, and recyclegas is outside furnace body through cooling
It removes and returns to furnace chamber after condensed water and carry out second-time burning, the gas of generation of burning contains first by second-time burning in recyclegas
The not sufficiently combusted combustion-supporting gas such as alkane, carbon monoxide realizes fully burning, and final tail gas is discharged by offgas outlet, in tail gas
Heat utilized by heat exchange, furnace cavity bottom burning generate solid slag be discharged by slag-drip opening, waste residue passes through separation
It can recycle, to realize that the solid-liquid-gas three phase product classification processing that incineration firing generates utilizes, reduce to the full extent
Environmental pollution in garbage processing procedure.
In the specific implementation mode in cooling water circulation path, the third cooling cavity, the second cooling cavity, institute
It states the first cooling cavity and passes sequentially through pipeline connection, greatly improve the heat utilization efficiency of cooling water, and by flow of cooling water
The optimization design in path ensures the cooling required of each cooling cavity.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto,
Any one skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (3)
1. a kind of solid-liquid-gas three phase product classification discharge refuse burner, which is characterized in that including：Combustion furnace, waste residue discharge dress
It sets, exhaust gas processing device (3), liquid waste treating apparatus；
Furnace interior has the furnace chamber for incineration firing, is equipped with garbage inlet at the top of the furnace chamber, the furnace cavity bottom is equipped with
Slag-drip opening, combustion furnace include upper furnace body (11) and lower furnace body (12)；
Upper furnace body (11) furnace wall includes wall and first time wall on first, and wall is set on first outside wall on second,
Wall has double-layer structure on first, is formed between the double-layer structure and recycles gas chamber, recycles gas chamber and is equipped with the
One import, first outlet, the second import, second outlet, the first import and second outlet are connected to furnace chamber, recycle in gas chamber
Equipped with cycle admission line (2), cycle admission line (2) both ends are connected to the second import and second outlet respectively, are enclosed on second
Wall is formed by the first tube body (4) coiled coil, and the two adjacent rings pipeline section of the first tube body (4) abuts against each other, the first tube body (4) both ends
It is respectively equipped with third import and third exports, form the first cooling cavity on first on wall and second between wall, first is cold
But cavity is equipped with the 4th import, the 4th outlet, and exhaust gas processing device (3) is described by pipeline and the 4th outlet
It is equipped with cooling pipe (5) in first cooling cavity, cooling medium is filled in cooling pipe (5)；
Lower furnace body (12) furnace wall includes first time coaming plate and second time coaming plate, and second time coaming plate is set in outside first time coaming plate,
The second cooling cavity is formed between first time coaming plate and second time coaming plate, and cooling medium is filled in the second cooling cavity,
Lower furnace body (12) furnace wall is equipped with air intake and offgas outlet, and the offgas outlet passes through pipeline and the 4th inlet communication；
Liquid waste treating apparatus includes cooler bin (61), circulating cooling pipe (62), waste collection slot, and circulating cooling pipe (62) setting exists
In cooler bin (61), circulating cooling pipe (62) both ends are connect with the second import and first outlet respectively, on circulating cooling pipe (62)
Equipped with the 5th outlet, waste collection slot and the 5th outlet；
Waste residue discharger is arranged at the slag-drip opening, and waste residue discharger includes multiple deslagging units, each deslagging unit
Including dregs discharge tube (71) and screw feed mechanism (72), have along the axially extending storage slag of dregs discharge tube (71) inside dregs discharge tube (71)
Cavity, dregs discharge tube (71) top have the first opening and are connected to the furnace chamber by first opening, dregs discharge tube (71) end
Portion is equipped with discharge port, and screw feed mechanism (72) is located in dregs discharge tube (71) and is axially arranged along dregs discharge tube (71).
2. solid-liquid-gas three phase product classification discharge refuse burner according to claim 1, which is characterized in that second outlet
It is equipped with recyclegas conduit (8), recyclegas conduit (8) is vertically arranged in the furnace chamber, and recyclegas conduit (8) is separate
The furnace chamber lower part is stretched into second outlet one end.
3. solid-liquid-gas three phase product classification discharge refuse burner according to claim 2, which is characterized in that recyclegas
Conduit (8) is located at far from second outlet one end above offgas outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610164162.8A CN105674294B (en) | 2016-03-21 | 2016-03-21 | A kind of solid-liquid-gas three phase product classification discharge refuse burner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610164162.8A CN105674294B (en) | 2016-03-21 | 2016-03-21 | A kind of solid-liquid-gas three phase product classification discharge refuse burner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105674294A CN105674294A (en) | 2016-06-15 |
| CN105674294B true CN105674294B (en) | 2018-09-11 |
Family
ID=56311417
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610164162.8A Active CN105674294B (en) | 2016-03-21 | 2016-03-21 | A kind of solid-liquid-gas three phase product classification discharge refuse burner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105674294B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114562730B (en) * | 2022-01-20 | 2024-06-28 | 广东绿富域资源再生科技有限公司 | Full-automatic intelligent household garbage incinerator |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2391101Y (en) * | 1999-07-14 | 2000-08-09 | 上海龙通环保设备有限公司 | Waste harmful gas energy-saving incinerator |
| JP4332768B2 (en) * | 2000-04-25 | 2009-09-16 | 株式会社Ｉｈｉ | Waste combustion equipment |
| CN2474908Y (en) * | 2001-03-05 | 2002-01-30 | 杨华平 | Straw gasification stove |
| JP2004156875A (en) * | 2002-11-08 | 2004-06-03 | Kangen Yoyu Gijutsu Kenkyusho:Kk | Waste disposing system |
| CN2697475Y (en) * | 2004-03-01 | 2005-05-04 | 天津大学 | Screened pyrolyzing treatment furnace for domestic refuse |
| CN105135437B (en) * | 2015-08-11 | 2018-05-29 | 李海平 | Weary gasification, burning integral type " three change " processing unit of house refuse and method |
| CN105202545A (en) * | 2015-09-25 | 2015-12-30 | 碧海舟（北京）节能环保装备有限公司 | Garbage pyrolysis gasification incineration treatment device |
| CN205619338U (en) * | 2016-03-21 | 2016-10-05 | 安徽未名生物环保有限公司 | Categorised discharge garbage combustion furnace of solid -liquid gas three -phase result |
-
2016
- 2016-03-21 CN CN201610164162.8A patent/CN105674294B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105674294A (en) | 2016-06-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104033271B (en) | A kind of efficient waste heat recycling system | |
| CN105385465A (en) | Garbage pyrolyzation device and method | |
| CN105674278B (en) | A kind of refuse burner of high combustion efficiency | |
| CN105674294B (en) | A kind of solid-liquid-gas three phase product classification discharge refuse burner | |
| CN205893035U (en) | Low heat value mud " three change " processing apparatus | |
| CN205619305U (en) | Garbage incinerator gas circulation device | |
| CN205619338U (en) | Categorised discharge garbage combustion furnace of solid -liquid gas three -phase result | |
| CN108613194A (en) | A kind of method and device for villages and small towns consumer waste incineration | |
| CN204153759U (en) | A kind of boiler residual heat recovery chamber | |
| CN213542428U (en) | Energy-concerving and environment-protective type biomass boiler | |
| CN205619271U (en) | Abundant domestic waste combustion apparatus burns | |
| CN105716085A (en) | Garbage treatment method | |
| CN105674277B (en) | A kind of incineration firing equipment of gas circulation | |
| CN106801875A (en) | A kind of recyclegas combustion-supporting type refuse disposal system | |
| CN205619270U (en) | Efficient gas endless waste combustion installation | |
| CN206803179U (en) | A kind of multi-chamber separating treatment refuse burning system | |
| CN105674279B (en) | A kind of sufficient house refuse combustion apparatus of burning | |
| CN108317720B (en) | Fuel oil boiler | |
| CN207159151U (en) | A kind of pyrolkigneous liquid collecting device | |
| CN205619280U (en) | Garbage combustion furnace that combustion efficiency is high | |
| CN205156000U (en) | Take dust collector's oil refining catalyst boiler tail gas waste heat recovery device | |
| CN207091365U (en) | A kind of Biohazard Waste gasification treatment device | |
| CN105674282B (en) | A kind of self-circulation type refuse treatment plant | |
| CN205619339U (en) | Gaseous heat exchange type garbage combustion furnace | |
| CN206430132U (en) | A kind of auxiliary heat type double-furnace-body double garbage burning system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211025 Address after: 418000 Huangbai village, Shuangjiang Town, Tongdao Dong Autonomous County, Huaihua City, Hunan Province (industrial concentration area) Patentee after: Hunan Weiming Environmental Protection Technology Co.,Ltd. Address before: 238000 Room 405, South fourth floor, Chaohu Economic Development Zone, Hefei, Anhui Province Patentee before: ANHUI WEIMING BIOLOGICAL ENVIRONMENTAL PROTECTION Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240602 Address after: Room 901, Zone 13, No. 1507 Fanghu Second Road, Huli District, Xiamen City, Fujian Province, 361000 Patentee after: Xiamen Weiming Environmental Protection Technology Co.,Ltd. Country or region after: China Address before: 418000 Huangbai village, Shuangjiang Town, Tongdao Dong Autonomous County, Huaihua City, Hunan Province (industrial concentration area) Patentee before: Hunan Weiming Environmental Protection Technology Co.,Ltd. Country or region before: China |