CN108561886A - A kind of horizontal domestic waste incineration - Google Patents
A kind of horizontal domestic waste incineration Download PDFInfo
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- CN108561886A CN108561886A CN201810692549.XA CN201810692549A CN108561886A CN 108561886 A CN108561886 A CN 108561886A CN 201810692549 A CN201810692549 A CN 201810692549A CN 108561886 A CN108561886 A CN 108561886A
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- Prior art keywords
- heat exchanger
- horizontal
- flue
- air heat
- air
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Classifications
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
- F23L15/04—Arrangements of recuperators
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
Abstract
The invention discloses a kind of horizontal domestic waste incinerations, it is characterised in that：Including burning furnace main body and heat-exchange system, the heat-exchange system includes main air heat exchanger, secondary air heat exchanger and hot-water heater, the top for burning furnace main body is equipped with multiple charge doors and heating air hose, it is equipped with ash discharge slope in the bottom for burning furnace main body, it is equipped with lower ash bucket in the top for receiving grey room, the side for burning furnace main body sets air-exchanging chamber, it is equipped with mixing chamber between air-exchanging chamber top and burning furnace main body, there are secondary air heat exchanger and gas heater in air-exchanging chamber, the other side is equipped with steam boiler, the flue of incinerator includes the horizontal flue and one section of vertical flue of two sections of Length discrepancies.The configuration of the present invention is simple, equipment investment is small, by air heating come combustion-supporting, reduces energy consumption, burns complete, can remove toxic dioxin peculiar smell.
Description
Technical field
The present invention relates to domestic rubbish disposals, more particularly to a kind of domestic waste incineration.
Background technology
In urbanization process, rubbish is many in the world as the burden that the product of Urban Metabolism was once urban development
There was the situation of garbage-surrounded city in city.And now rubbish is considered as most " urban ore
Hide ", it is " resource mislayed ".This is both deep and in-depth and urban development the inevitable requirement recognized rubbish.In
State's domestic rubbish disposal mainly based on sanitary landfills, accounts for 78% for the treatment of capacity or so, and garbage classification subdivision is not at this stage
By force, the route relatively efficiently recycled is not formed.
China's domestic rubbish disposal is in many ground for needing specification compared with the primary stage from source to final processing
Side, such as classify, recycle, processing mode.Present stage of china is primarily directed to the processing for having generated rubbish, for similar beautiful
The theory of state's control rubbish source of generation does not embody in technology path, and the mode handled is relatively single, mainly
It is the mode of sanitary landfills, since classification does not refine, causes the recovery utilization rate of resource very low.
The development of China's domestic rubbish disposal in recent years is very fast, ends 2010, China's Output of Domestic Waste reaches 2.51
Hundred million tons, and the amount of clearing is 1.58 hundred million tons, is equivalent to the 62.94% of yield, treating capacity is 1.23 hundred million tons, is equivalent to yield
49%, the 77.85% of the amount of clearing, the nearly house refuse of half is also very big all in untreated or simply dealt state
Room for promotion.
Waste incineration is a kind of method of more ancient traditional processing rubbish, after being handled with burning method due to rubbish, is subtracted
Quantification effect is notable, saves land used, can also eliminate various pathogen, convert poisonous and harmful substance to harmless object, therefore rubbish is burnt
Burning method has become one of main method for the treatment of of urban garbage.
But it builds a large and medium-sized incinerator and wants 1,000,000,000 yuans easily, the processing cost of the environmental protection after being constructed and put into operation is big
300 yuan/ton are about needed, at present the operating method of the country's that one ton of house refuse of dozens of yuan incineration disposal of some cities, if true
It is that handle itself all by environmentally friendly program be suspectable.The general city of incineration treatment method of environmental protection is difficult to bear.
It needs to frequently replace filtering adsorbing material in running, and also spends overspending, often causes to operate arbitrarily simplified loophole.
The incineration technology of traditional type is since ventilation fire resisting cylinder, fire resisting cylinder connector are all more, and fragile, effect is poor, high energy consumption.Either with resistance to
The accumulation of heat of firebrick, per half an hour, conversion is primary, inconvenient for operation, dangerous big.Incinerator is mostly vertical incinerator simultaneously, is existed
There is cooling fast, temperature liter is not high, and energy consumption is also high, and inconvenient for operation.
And incineration flue gas of household garbage Zhong bioxin be in recent years countries in the world institute general concern the problem of.Er Evil
English class extremely toxic substance causes very big harm to environment, effectively controls the generation and diffusion of dioxins materials, is directly related to rubbish
Rubbish burns and the promotion and application of Waste Firing Power Generation Technique.
Invention content
The present invention is for disadvantage present in background technology and problem is improved and innovated, and it is an object of the present invention to provide a kind of knot
Structure is simple, and equipment investment is small, by air heating come combustion-supporting, reduces energy consumption, burn it is complete, can be clear by toxic dioxin peculiar smell
The horizontal domestic waste incineration removed.
The technical solution adopted by the present invention is as follows：A kind of horizontal domestic waste incineration, it is characterised in that：Including incinerator
Main body and heat-exchange system, the heat-exchange system include main air heat exchanger, secondary air heat exchanger, hot-water heater and coal gas
Heater, the top for burning furnace main body are equipped with multiple charge doors, are equipped with heating air hose in the lower section of charge door, heating is empty
Multiple heating air tube inlets are provided on tracheae, being equipped with the coke that will be burnt and tie in the lower section of corresponding charge door in heating air hose beats
Scattered block hitting device, ash discharge slope is equipped in the bottom for burning furnace main body, and lower ash bucket, incinerator master are equipped in the top for receiving grey room
The side of body sets air-exchanging chamber, and mixing chamber is equipped between air-exchanging chamber top and burning furnace main body, has secondary air heat exchange in air-exchanging chamber
Device and gas heater, the other side are equipped with steam boiler, the flue of incinerator include two sections of Length discrepancies horizontal flue and one section
Vertical flue, wherein short horizontal flue from burn furnace main body top come out, connect vertical flue, then connect positioned at burn furnace main body and
The long horizontal flue of the bottom part down of secondary air heat exchanger is equipped with main air heat exchanger, vertical in long horizontal flue
Flue is arranged right below hot-water heater, and hot-water heater and steam boiler form circulating-heating；The main air heat exchanger
Outlet be connected with the import of secondary air exchanger base, the one outlet of secondary air heat exchanger connects mixing chamber, another
Outlet connects heating air hose, and thermocouple is housed at secondary air heat exchanger exit.
The pipeline of the hot-water heater is wolfram steel pipe, and the pipeline of main air heat exchanger and secondary air heat exchanger is steel
Pipe.
The hot-water heater, main air heat exchanger, secondary air heat exchanger and gas heater structure have two
Item horizontal supervisor setting up and down, air inlet pipe are responsible for for lower horizontal, and escape pipe is responsible for for upper horizontal, described two horizontal supervisors
Between be connected directly by a plurality of VERTICAL TUBE, and secondly side is first come out by curved pipe, then curved pipe is connected with VERTICAL TUBE.
The vertical flue is divided into 4 long horizontal flues in bottom, and the long horizontal flue is all connected with air-exchanging chamber, every
Main air heat exchanger is respectively housed, the secondary air heat exchanger is also 4 groups, a main air heat exchanger in long horizontal flue
Outlet connect the import of a secondary air heat exchanger.
The long horizontal flue has multiple repair entrances air-exchanging chamber.
The incinerator body top is arch form.
The long horizontal flue is arch form.
The flue gas of the present invention comes out from the short horizontal flue at the top for burning furnace main body, and flue-gas temperature is about 1000 DEG C, by
Vertical flue is downward, and steam is generated by the cold water in heat hot water heater, realizes and cools down for the first time, and temperature is 600 ~ 700
℃；Main air heat exchanger heat exchange through long horizontal flue again preheats oxygen-enriched air for the first time；Pass through two level in air-exchanging chamber again
Air heat exchanger preheats oxygen-enriched air and by heated by gas pipe heating gas to 300 ~ 500 DEG C for second, goes out by flue
Mouth discharge, discharge flue-gas temperature are 300 ~ 500 DEG C.Oxygen-enriched air exchanges heat through main air heat exchanger, then exchanges heat through secondary air
Device exchanges heat, and a part of oxygen-enriched air is mixed in mixing chamber with coal gas, and through burning torch ignition, combustion flame continuation, which is arrived forward, to be added
Warm-air pipe exit；The heated air hose of another part oxygen-enriched air is sent out, and the rubbish of addition mixes, and combustion flame will mix
The rubbish after oxygen-enriched air is closed to light；Ash after incineration firing is collected through lower ash bucket, is slowly piled up on ash discharge slope, then by ash discharge
Slope is discharged.
Furnace main body to be burned when beginning to use, first passes through closed furnace door, Control for Kiln Temperature is burnt 2 ~ 3 days at 200 ~ 300 DEG C,
It is warming up to after 500 ~ 600 DEG C and burns again 2 ~ 3 days again, ignition temperature is then risen to 800 ~ 1200 DEG C again, then control 800 ~
It burns under the conditions of 1200 DEG C, can effectively control the generation and diffusion of dioxins materials；Flue gas is dropped through hot-water heater simultaneously
Temperature is to after 600 ~ 700 DEG C, then is sent to main air heat exchanger, secondary air heat exchanger, gas heater heat exchange, temperature in steel pipe
550 DEG C are not above, can not only utilize the excellent heat exchange property of steel pipe, but also can prevent steel pipe from being damaged because temperature is excessively high.
The configuration of the present invention is simple, equipment investment is small, and by air heating come combustion-supporting, reduction energy consumption, completely, energy will have for burning
The dioxin peculiar smell of poison is removed.
Description of the drawings
Fig. 1 is the structural schematic diagram of the present invention；
Fig. 2 is the pipeline configuration schematic diagram of air heat exchanger pipeline；
Fig. 3 is the pipeline configuration schematic diagram of the hot device of coal gas；
In figure：1 is air-exchanging chamber, and 2 be burning torch, and 3 be mixing chamber, and 4 be hot air inlet, and 5 be heating air intake, and 6 are
Charge door, 7 be heating air hose, and 8 be furnace roof, and 9 be flue, and 10 be insulated wall, and 11 be cooling mouth, and 12 be cool air inlet, 13
It is lower ash bucket, 14 be block hitting device, and 15 be First Heat Exchanger, and 16 be fire hole, and 17 be heating gas entrance, and 18 be ash retaining wall, 19
It is repair entrance, 20 be flue outlet, and 21 be steam boiler, and 22 be the second heat exchanger, and 23 be gas heater, and 24 be cold air
Import, 25 be hot-air inlets, and 26 be cooled coal gas import, and 27 be heating gas import.
Specific implementation mode
Below according to the drawings and specific embodiments, the invention will be further described：
From fig. 1, it can be seen that the present invention is a kind of horizontal domestic waste incineration, including burns furnace main body and heat-exchange system, it is described to change
Hot systems include main air heat exchanger, secondary air heat exchanger, hot-water heater and gas heater, incinerator body top
For arch form, multiple charge doors are equipped at the top for burning furnace main body, heating air hose is equipped in the lower section of charge door, heats air
It is provided with multiple heating air tube inlets on pipe, corresponds to be equipped at charge door in the lower section of heating air hose and breaks up the coke of burning knot
Block hitting device, be equipped in the bottom for burning furnace main body and receive grey room, be equipped with lower ash bucket in the top for receiving grey room, burn furnace main body
Side sets air-exchanging chamber, air-exchanging chamber top and burns and is equipped with mixing chamber between furnace main body, have in air-exchanging chamber secondary air heat exchanger and
Gas heater, the other side are equipped with steam boiler, the flue of incinerator include two sections of Length discrepancies horizontal flue and one section it is vertical
Flue connects vertical flue wherein short horizontal flue comes out from the top for burning furnace main body, then connects positioned at burning furnace main body and two level
The long horizontal flue of the bottom part down of air heat exchanger, long horizontal flue are arch form, and main air is equipped in long horizontal flue
Heat exchanger is arranged right below hot-water heater in vertical flue, and hot-water heater and steam boiler form circulating-heating；Described one
The outlet of grade air heat exchanger is connected with the import of secondary air exchanger base, and the one outlet of secondary air heat exchanger is opened in
In mixing chamber, another outlet connects heating air hose, and thermocouple is housed at secondary air heat exchanger exit.The horizontal cigarette of the length
Road has multiple repair entrances air-exchanging chamber.
The pipeline of the hot-water heater is wolfram steel pipe, and the pipeline of main air heat exchanger and secondary air heat exchanger is steel
Pipe.The main air heat exchanger and secondary air heat exchanger are respectively 4 groups, and a main air heat exchanger corresponds to a two level sky
Gas heat exchanger.From Fig. 2,3 it is found that the hot-water heater, main air heat exchanger, secondary air heat exchanger and gas heater
Structure to have two horizontal supervisors setting up and down, air inlet pipe be that lower horizontal is responsible for, escape pipe is upper horizontal supervisor,
It is connected directly by a plurality of VERTICAL TUBE between the two horizontal supervisor, and secondly side is first come out by curved pipe, then will with VERTICAL TUBE
Curved pipe connects.It is equipped with explosion-proof pad in lower horizontal supervisor's entrance of gas heater.
The vertical flue is divided into 4 long horizontal flues in bottom, and the long horizontal flue is all connected with air-exchanging chamber, every
Main air heat exchanger is respectively housed, the secondary air heat exchanger is also 4 groups, a main air heat exchanger in long horizontal flue
Outlet connect the import of a secondary air heat exchanger.
The flue gas of the present invention comes out from the short horizontal flue at the top for burning furnace main body, downward by vertical flue, by adding
Cold water in hot hot-water heater generates steam, realizes and cools down for the first time；The main air heat exchanger through long horizontal flue changes again
Heat preheats oxygen-enriched air for the first time；Oxygen-enriched air is preheated for second by secondary air heat exchanger in air-exchanging chamber again, by
Flue outlet is discharged.Oxygen-enriched air exchanges heat through main air heat exchanger, then exchanges heat through secondary air heat exchanger, a part of oxygen-enriched sky
Gas is mixed in mixing chamber with coal gas, and through burning torch ignition, combustion flame continuation is arrived forward at heating air hose；Another part
The heated air hose of oxygen-enriched air is sent out, and the rubbish of addition mixes, and combustion flame lights the rubbish after mixing oxygen-enriched air；
Ash after incineration firing is collected through lower ash bucket, is slowly piled up on ash discharge slope, then be discharged by ash discharge slope.
Furnace main body to be burned when beginning to use, first passes through closed furnace door, Control for Kiln Temperature is burnt 2 ~ 3 days at 200 ~ 300 DEG C,
It is warming up to after 500 ~ 600 DEG C and burns again 2 ~ 3 days again, ignition temperature is then risen to 800 ~ 1200 DEG C again, then control 800 ~
It burns under the conditions of 1200 DEG C, can effectively control the generation and diffusion of dioxins materials；Flue gas is dropped through hot-water heater simultaneously
Temperature is to after 600 ~ 700 DEG C, then is sent to main air heat exchanger, secondary air heat exchanger, gas heater heat exchange, temperature in steel pipe
550 DEG C are not above, can not only utilize the excellent heat exchange property of steel pipe, but also can prevent steel pipe from being damaged because temperature is excessively high.
Embodiment of the present invention is only the description carried out to the preferred embodiment of invention, not to structure of the present invention
Think and range is defined, under the premise of not departing from invention design philosophy, engineers and technicians are to the present invention's in this field
The all variations and modifications that technical solution is made, should all fall into protection scope of the present invention, in the claimed technology of the present invention
Hold, has all recorded in detail in the claims.
Claims (9)
1. a kind of horizontal domestic waste incineration, it is characterised in that：Including burning furnace main body and heat-exchange system, the heat-exchange system
Including main air heat exchanger, secondary air heat exchanger, hot-water heater and gas heater, the top for burning furnace main body
Equipped with multiple charge doors, it is equipped with heating air hose in the lower section of charge door, being provided with multiple heating air hoses on heating air hose enters
Mouthful, the block hitting device for breaing up the coke of burning knot is equipped in the lower section of corresponding charge door in heating air hose, is burning furnace main body
Bottom be equipped with ash discharge slope, be equipped with lower ash bucket in the top for receiving grey room, the side for burning furnace main body sets air-exchanging chamber, on air-exchanging chamber
It is equipped with mixing chamber between portion and burning furnace main body, has secondary air heat exchanger and gas heater, the other side to be equipped in air-exchanging chamber
Steam boiler, the flue of incinerator include the horizontal flue and one section of vertical flue of two sections of Length discrepancies, wherein short horizontal flue from
The top for burning furnace main body comes out, and connects vertical flue, then connects positioned at the bottom part down for burning furnace main body and secondary air heat exchanger
Long horizontal flue, in long horizontal flue be equipped with main air heat exchanger, be arranged right below hot-water heater in vertical flue,
Hot-water heater and steam boiler form circulating-heating；The outlet of the main air heat exchanger and secondary air exchanger base
Import be connected, the one outlet of secondary air heat exchanger is opened in mixing chamber, another outlet connects heating air hose, and two level is empty
Thermocouple is housed at gas heat exchanger exit.
2. horizontal domestic waste incineration according to claim 1, it is characterised in that：The pipeline of the hot-water heater is
The pipeline of wolfram steel pipe, main air heat exchanger and secondary air heat exchanger is steel pipe.
3. according to any horizontal domestic waste incineration of claim 1,2, it is characterised in that：The hot-water heater,
The structure of main air heat exchanger, secondary air heat exchanger and gas heater has two horizontal supervisors setting up and down,
Air inlet pipe is responsible for for lower horizontal, and escape pipe is responsible for for upper horizontal, direct by a plurality of VERTICAL TUBE between described two horizontal supervisors
It is connected, and secondly side is first come out by curved pipe, then is connected curved pipe with VERTICAL TUBE.
4. horizontal domestic waste incineration according to claim 1, it is characterised in that：The vertical flue is divided into bottom
4 long horizontal flues, the long horizontal flue are all connected with air-exchanging chamber, and main air is respectively housed in every long horizontal flue and is exchanged heat
Device, the secondary air heat exchanger are also 4 groups, the outlet of a main air heat exchanger connect secondary air heat exchanger into
Mouthful.
5. horizontal domestic waste incineration according to claim 1, it is characterised in that：The long horizontal flue is being taken a breath
Room has multiple repair entrances.
6. horizontal domestic waste incineration according to claim 1, it is characterised in that：The incinerator body top is arch
Type.
7. horizontal domestic waste incineration according to claim 1, it is characterised in that：The long horizontal flue is arch form.
8. horizontal domestic waste incineration according to claim 1, it is characterised in that：Furnace main body is burned to begin to use
When, closed furnace door is first passed through, Control for Kiln Temperature is burnt 2 ~ 3 days at 200 ~ 300 DEG C, then burns 2 ~ 3 after being warming up to 500 ~ 600 DEG C again
It, then rises to 800 ~ 1200 DEG C by ignition temperature again, then controls and burn under the conditions of 800 ~ 1200 DEG C；Flue gas is through hot water simultaneously
After heater is cooled to 600 ~ 700 DEG C, then it is sent to main air heat exchanger, secondary air heat exchanger, gas heater heat exchange.
9. horizontal domestic waste incineration according to claim 3, it is characterised in that：The lower section water of the gas heater
The entrance of flat supervisor is equipped with explosion-proof pad.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810692549.XA CN108561886A (en) | 2018-06-29 | 2018-06-29 | A kind of horizontal domestic waste incineration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810692549.XA CN108561886A (en) | 2018-06-29 | 2018-06-29 | A kind of horizontal domestic waste incineration |
Publications (1)
| Publication Number | Publication Date |
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| CN108561886A true CN108561886A (en) | 2018-09-21 |
Family
ID=63554950
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| Application Number | Title | Priority Date | Filing Date |
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| CN201810692549.XA Pending CN108561886A (en) | 2018-06-29 | 2018-06-29 | A kind of horizontal domestic waste incineration |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1163440A (en) * | 1997-08-12 | 1999-03-05 | Asada Shokai:Kk | Waste incinerator |
| CN101706106A (en) * | 2009-11-26 | 2010-05-12 | 创冠环保(中国)有限公司 | Recovering device for afterheat of garbage incineration furnace |
| CN102042598A (en) * | 2011-01-25 | 2011-05-04 | 伟明环保设备有限公司 | Horizontal garbage incinerator |
| CN102183025A (en) * | 2011-05-10 | 2011-09-14 | 李凤山 | Urban garbage incinerating boiler |
| JP2012013315A (en) * | 2010-06-30 | 2012-01-19 | Oono Kaihatsu Kk | Refuse incineration equipment |
| CN105972605A (en) * | 2016-03-29 | 2016-09-28 | 东南大学 | Small household garbage incineration treatment system and incineration treatment method |
| CN206846724U (en) * | 2017-05-02 | 2018-01-05 | 禹旭东 | A kind of horizontal incinerator |
| CN108006640A (en) * | 2017-12-21 | 2018-05-08 | 靖江博鑫柯曼燃烧器制造有限公司 | One kind uses oxygen-enriched burner |
-
2018
- 2018-06-29 CN CN201810692549.XA patent/CN108561886A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1163440A (en) * | 1997-08-12 | 1999-03-05 | Asada Shokai:Kk | Waste incinerator |
| CN101706106A (en) * | 2009-11-26 | 2010-05-12 | 创冠环保(中国)有限公司 | Recovering device for afterheat of garbage incineration furnace |
| JP2012013315A (en) * | 2010-06-30 | 2012-01-19 | Oono Kaihatsu Kk | Refuse incineration equipment |
| CN102042598A (en) * | 2011-01-25 | 2011-05-04 | 伟明环保设备有限公司 | Horizontal garbage incinerator |
| CN102183025A (en) * | 2011-05-10 | 2011-09-14 | 李凤山 | Urban garbage incinerating boiler |
| CN105972605A (en) * | 2016-03-29 | 2016-09-28 | 东南大学 | Small household garbage incineration treatment system and incineration treatment method |
| CN206846724U (en) * | 2017-05-02 | 2018-01-05 | 禹旭东 | A kind of horizontal incinerator |
| CN108006640A (en) * | 2017-12-21 | 2018-05-08 | 靖江博鑫柯曼燃烧器制造有限公司 | One kind uses oxygen-enriched burner |
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Application publication date: 20180921 |
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