CN206919025U - A kind of combined type incinerator - Google Patents
A kind of combined type incinerator Download PDFInfo
- Publication number
- CN206919025U CN206919025U CN201720793597.9U CN201720793597U CN206919025U CN 206919025 U CN206919025 U CN 206919025U CN 201720793597 U CN201720793597 U CN 201720793597U CN 206919025 U CN206919025 U CN 206919025U
- Authority
- CN
- China
- Prior art keywords
- fluidized bed
- burner
- incinerator
- bed incinerator
- combined type
- 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
Landscapes
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
The utility model discloses a kind of combined type incinerator, including：Rotation error, fluidized bed incinerator and the burner of Horizontal sedimentation two, the Rotation error connect fluidized bed incinerator, and the fluidized bed incinerator connects the burner of Horizontal sedimentation two.The beneficial effects of the utility model are：The pre-treatment working strength that solid waste is burned is reduced, need to only control the content of melt substance to enter stove by simple compatibility and burn；Because fluid bed furnace has shared part burning amount, the body of heater of kiln is caused to reduce when production capacity is constant；When carrying out dangerous solid waste burning, kiln incineration temperature is directly risen to 1100 DEG C, saves secondary combustion-supporting fuel；The burner of Horizontal sedimentation two provides two enough combustion spaces, it is ensured that gas residence time, realizes the function of chalk dust removing again.
Description
Technical field
The incineration treatment technology field of solid waste (thing containing dangerous waste) is the utility model is related to, more particularly to a kind of combined type burns
Burn device.
Background technology
Solid waste (thing containing dangerous waste) usually needs to carry out processing disposal using burning.To prevent solid waste (thing containing dangerous waste) from burning
Secondary pollution is produced during burning, country fires temperature and residence time etc. to the temperature of burning, burnout rate, flue gas two and is made that sternly
The regulation of lattice.
Rotation error is because it can adapt to the burning of various fuel, all kinds of solid wastes, and incineration temperature can be up to
More than 1100 DEG C, it is widely used in the burning of all types of industries solid waste, rubbish, sludge etc., and dangerous waste is burned.Burned using following current
Mode, by controlling solid waste furnace entering volume, fuel dosage, air blast air quantity, kiln rotating speed etc., it is possible to achieve needed for solid waste burning
Temperature, residence time, ensure the burnout rate of solid waste；Two burners are connected after Rotation error and design enough capacity, can
To realize that sufficient flue gas two fires.
Varied due to entering stove solid waste, it is very big that solid waste burns required time difference, is easily made with stepping into when stove burns
It is low into burnout rate, do not meet the requirement of national standard.Therefore, some knockdown incinerating methods are created, such as：Chinese patent
CN202792039U discloses a kind of hazardous Waste Incineration technology, the technology remain rotary kiln it is adaptable,
On the basis of stable and reliable operation, secondary burning is carried out by the flue gas discharged using grate furnace to rotary kiln, rotary kiln is arranged
The waste residue gone out carries out sustained combustion；Chinese patent CN103542415A discloses a kind of combined type sludge incineration device, including returns
Rotatable pyrolysis installation, incinerator, waste heat boiler, air preheater and cigarette wind matching device.Patent collection kiln, the pyrolysis gas
Change stove, reciprocating grate furnace advantage, swinging pyrolysis gasification furnace therein is accompanied by cigarette wind matching device, using flow,
The controllable mixture cigarette wind of temperature, oxygen content, to entering pyrolytic gasification and the anoxycausis that stove sludge is stablized, in its pyrolytic process
For caused fuel gas in the presence of system negative pressure, the dual firing chamber into incinerator carries out high temperature incineration processing, the combustion of its anoxic
The solid fraction sludge not burnt during burning, falls directly into and continues burning disposal on the reciprocal grate of incinerator.
Above-mentioned two patent solves the problems, such as burnout rate to a certain extent, but can not catch the dust settling in flue gas
Collection.Solid waste burning technical specification and standard requirement by national regulation, flying dust caused by solid waste (containing dangerous waste) burning are considered
Dangerous waste is, it is necessary to specially treated.Because Rotation error burner hearth wind speed is higher, substantial amounts of solid particle is mixed with caused flue gas
Thing, wherein the dust such as the existing solid waste molecule not burnt, fine slag, also there is the flying dust for having adsorbed numerous pollutants.All
Trap to form flying dust by dedusting, flying dust amount can be caused to increase severely, processing cost of disposal is high.
The content of the invention
The purpose of this utility model is to provide one kind in place of overcome the deficiencies in the prior art and be used for solid waste including danger
Dangerous waste is fully burnt, flue gas two fires and dust catching once burns the combined type incinerator of completion.
In order to solve the above-mentioned technical problem, the technical solution adopted in the utility model is：A kind of group for incinerating method
Box-like incinerator, including：Rotation error, fluidized bed incinerator and the burner of Horizontal sedimentation two, the Rotation error
Fluidized bed incinerator is connected, the fluidized bed incinerator connects the burner of Horizontal sedimentation two.
The Rotation error and fluidized bed incinerator directly in conjunction with：The fluidized bed incinerator fires with Horizontal sedimentation two
Stove directly in conjunction with.
The fluidized bed incinerator side connects with the Rotation error, receive Rotation error from top to bottom from
What kiln hood to kiln tail was fallen into does not burn waste；The opposite side of the fluidized bed incinerator connects with the burner of Horizontal sedimentation two,
Flue gas is delivered to the burning of the burner of Horizontal sedimentation two.
The burner stage casing of Horizontal sedimentation two is provided with ammonia atomization nozzle, to furnace injection ammoniacal liquor.
Dust settling capturing device is provided with the burner of Horizontal sedimentation two.
The fluidized bed incinerator top is provided with post-blast device.
The fluidized bed incinerator top is provided with burner.
The beneficial effects of the utility model are：1) reduce the pre-treatment working strength of solid waste burning, only need to pass through letter
Single compatibility is burned with controlling the content of melt substance to enter stove.Wherein inflammable material is filled in Rotation error
Divide burning disposal, produce a small amount of lime-ash and enter fluid bed furnace.Because nonflammable material passes through the burning of kiln for a period of time
Afterwards, enter back into fluid bed furnace and continue to burn, the burnout rate of nonflammable material can be improved, it is ensured that production capacity or increase production capacity.
2) because fluid bed furnace has shared part burning amount, the body of heater of kiln is caused to reduce when production capacity is constant, together
When a kiln air blast reduce, air distribution coefficient is 1.0~1.2；Fluid bed furnace increases post-blast, and air distribution coefficient is 1.6
~2.0, it is ensured that two combustions of residue and flue gas so that the air distribution of burning process more conforms to the low air distribution of kiln and fluid bed furnace
The combustion characteristics of high air distribution.
3) when carrying out dangerous solid waste burning, kiln incineration temperature directly can be risen to 1100 DEG C；Into fluidisation
After pool furnace, residue falls into the fluid bed furnace of lower position, under the effect of fluid bed furnace air distribution temperature decline and maintain 900 DEG C
Continue to burn；1100 DEG C of high-temperature flue gas directly enters the burner of Horizontal sedimentation two from fluid bed furnace top, is matched somebody with somebody by post-blast
Than making fuel gas therein etc. fully burn, and 1100 DEG C of burning is maintained, save secondary combustion-supporting fuel.Similarly, carrying out
When general solid waste is burned, it can also cancel secondary combustion-supporting.
4) two burners with Horizontal sedimentation structure provide two enough combustion spaces, it is ensured that gas residence time, and it is real
The function of chalk dust removing is showed.
Brief description of the drawings
Fig. 1 is combined type incinerator schematic diagram of the present utility model.
Wherein：
1st, Rotation error 2, fluidized bed incinerator 3, the burner of Horizontal sedimentation two
Embodiment
The utility model is described in further detail with reference to the accompanying drawings and detailed description：
A kind of combined type incinerator as shown in Figure 1, including：Rotation error 1, fluidized bed incinerator 2 and horizontal heavy
Two burners 3 drop, and Rotation error 1 is directly in conjunction with fluidized bed incinerator 2, and fluidized bed incinerator 2 is directly in conjunction with Horizontal sedimentation two
Burner 3.The side of fluidized bed incinerator 2 connects with the Rotation error 1, receives Rotation error 1 from top to bottom from kiln
Head does not burn waste to what kiln tail was fallen into；The opposite side of fluidized bed incinerator 2 connects with the burner 3 of Horizontal sedimentation two, and flue gas is defeated
The burner 3 of Horizontal sedimentation two is delivered to burn.
The top of fluidized bed incinerator 2 is provided with post-blast device and burner, is fired for flue gas two；The burner of Horizontal sedimentation two
Dust settling capturing device is provided with 3；The stage casing of two burner of Horizontal sedimentation 3 is provided with ammonia atomization nozzle, enters to furnace injection ammoniacal liquor
Row SNCR processing.
Comprised the following steps using the incinerating method of said apparatus, 1) input solid waste from Rotation error kiln hood,
Ignite, and with the rotation of kiln, burn while flowing to kiln tail；2) residue outflow kiln tail, falls into fluidized bed incinerator
Continue to burn, burn rear clinker discharge；3) flue gas enters the combustion of the burner of Horizontal sedimentation two progress two, while the dust in flue gas is sunk
Drop trapping, delivers to incinerator and burns again.
Embodiment one：
When carrying out general solid waste burning processing, the device is run in accordance with the following methods：
1) by solid waste from the input of the kiln hood of Rotation error 1, ignite, and with the rotation of kiln 1, burn while
Flow to kiln tail.By combustion-supporting fuel, kiln air blast, the control of solid waste amount, it is 900 DEG C to maintain burner hearth incineration temperature, and is led to
Cross the rotating speed of control Rotation error 1 and burn the residence time about 60min to control；
2) residue outflow kiln tail, falls into fluidized bed incinerator 2 and continues to burn, and is controlled by the air distribution of fluidized bed incinerator 2
Incineration temperature is 900 DEG C, burns residence time about 30min, and then clinker is discharged；
3) flue gas enters the combustion of the burner 3 of Horizontal sedimentation two progress two from the top of fluidized bed incinerator 2, and matches somebody with somebody air control by two combustions
Incineration temperature processed is 900 DEG C, and flue gas two fires residence time >=2s, while the dust settling in flue gas is trapped；
4) ammonia atomization nozzle is installed in the stage casing of two burner of Horizontal sedimentation 3, to furnace injection ammoniacal liquor, can carries out taking off in stove
Nitre.
Embodiment two：
When carrying out dangerous solid waste burning processing, the device is run in accordance with the following methods：
1) by solid waste from the input of the kiln hood of Rotation error 1, ignite, and with the rotation of kiln 1, burn while
Flow to kiln tail.By combustion-supporting fuel, an air blast, the control of solid waste amount, it is 1100 DEG C to maintain burner hearth incineration temperature, and passes through control
The rotating speed of Rotation error 1 processed burns the residence time about 60min to control；
2) residue outflow kiln tail, falls into fluidized bed incinerator 2 and continues to burn, and is controlled by the air distribution of fluidized bed incinerator 2
Incineration temperature is 900 DEG C, burns residence time about 30min, and then clinker is discharged；
3) flue gas enters the combustion of the burner 3 of Horizontal sedimentation two progress two from the top of fluidized bed incinerator 2, and matches somebody with somebody air control by two combustions
Incineration temperature processed is 1100 DEG C, two combustion residence time >=2s, while the dust settling in flue gas is trapped；
4) ammonia atomization nozzle is installed in the stage casing of two burner of Horizontal sedimentation 3, to furnace injection ammoniacal liquor, can carries out taking off in stove
Nitre.
Claims (7)
1. a kind of combined type incinerator, including：Rotation error (1), fluidized bed incinerator (2) and the burner of Horizontal sedimentation two
(3), it is characterized in that：Rotation error (1) the connection fluidized bed incinerator (2), fluidized bed incinerator (2) connection are sleeping
Formula settles two burners (3).
2. combined type incinerator according to claim 1, it is characterized in that：The Rotation error (1) and fluid bed
Incinerator (2) directly in conjunction with：The fluidized bed incinerator (2) and the burner of Horizontal sedimentation two (3) directly in conjunction with.
3. combined type incinerator according to claim 1 or 2, it is characterized in that：Fluidized bed incinerator (2) side with
The Rotation error (1) connection, it is useless from not burning of falling into of kiln hood to kiln tail from top to bottom to receive Rotation error (1)
Thing；The opposite side of the fluidized bed incinerator (2) connects with the burner of Horizontal sedimentation two (3), and it is horizontal heavy that flue gas is delivered to
Two burners (3) burning is dropped.
4. combined type incinerator according to claim 3, it is characterized in that：The burner of Horizontal sedimentation two (3) stage casing is set
There is ammonia atomization nozzle, to furnace injection ammoniacal liquor.
5. combined type incinerator according to claim 3, it is characterized in that：It is provided with the burner of Horizontal sedimentation two (3)
Dust settling capturing device.
6. combined type incinerator according to claim 3, it is characterized in that：Fluidized bed incinerator (2) top is provided with
Post-blast device.
7. combined type incinerator according to claim 3, it is characterized in that：Fluidized bed incinerator (2) top is provided with
Burner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720793597.9U CN206919025U (en) | 2017-07-03 | 2017-07-03 | A kind of combined type incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720793597.9U CN206919025U (en) | 2017-07-03 | 2017-07-03 | A kind of combined type incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206919025U true CN206919025U (en) | 2018-01-23 |
Family
ID=61335589
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720793597.9U Active CN206919025U (en) | 2017-07-03 | 2017-07-03 | A kind of combined type incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206919025U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107178786A (en) * | 2017-07-03 | 2017-09-19 | 天津市美好生活科技有限公司 | A kind of incinerating method and combinations thereof formula incinerator |
| CN111006217A (en) * | 2019-12-30 | 2020-04-14 | 合肥工业大学 | Energy-concerving and environment-protective hazardous waste processing system |
| CN111288454A (en) * | 2020-03-03 | 2020-06-16 | 合肥工业大学 | High-efficient clean charcoal gas coproduction device |
| CN113970101A (en) * | 2020-07-22 | 2022-01-25 | 中冶长天国际工程有限责任公司 | Hazardous waste pyrolysis incineration system and temperature control method thereof |
-
2017
- 2017-07-03 CN CN201720793597.9U patent/CN206919025U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107178786A (en) * | 2017-07-03 | 2017-09-19 | 天津市美好生活科技有限公司 | A kind of incinerating method and combinations thereof formula incinerator |
| CN111006217A (en) * | 2019-12-30 | 2020-04-14 | 合肥工业大学 | Energy-concerving and environment-protective hazardous waste processing system |
| CN111006217B (en) * | 2019-12-30 | 2022-02-11 | 合肥工业大学 | Energy-concerving and environment-protective hazardous waste processing system |
| CN111288454A (en) * | 2020-03-03 | 2020-06-16 | 合肥工业大学 | High-efficient clean charcoal gas coproduction device |
| CN113970101A (en) * | 2020-07-22 | 2022-01-25 | 中冶长天国际工程有限责任公司 | Hazardous waste pyrolysis incineration system and temperature control method thereof |
| CN113970101B (en) * | 2020-07-22 | 2023-06-23 | 中冶长天国际工程有限责任公司 | Dangerous waste pyrolysis incineration system and temperature control method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105509062B (en) | Full size electronic apparatus discarded object continuous pyrolysis incinerator | |
| CN206919025U (en) | A kind of combined type incinerator | |
| CN102607033B (en) | One way of life refuse gasification melting incineration system and incinerating method thereof | |
| CN200958757Y (en) | Vertical thermal-decomposition incinerator | |
| CN101398168A (en) | Method and apparatus for operating a fuel flexible furnace to reduce pollutants in emissions | |
| CN105889933A (en) | Garbage incinerating device and method for conducting deacidification in garbage incinerator | |
| CN206094112U (en) | Sludge incineration system | |
| CN201666719U (en) | Coal dust hot-air furnace system of spray dryer | |
| CN102221210B (en) | Low temperature discharge system for disposing multi-dimensional chemistry waste burning and recovering afterheat smoke | |
| CN108559546B (en) | Household garbage pyrolysis treatment method and pyrolysis treatment system | |
| CN100432532C (en) | Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator | |
| CN205316333U (en) | Device is burned in continuous pyrolysis of full -scale electronic apparatus discarded object | |
| CN206739283U (en) | A kind of depth peak regulation preheats low-load combustion-stabilizing combustion system with heat smoke | |
| CN106402894A (en) | Large-size hazardous waste rotary kiln type incinerator device taking sludge as main target | |
| CN201462862U (en) | Waste gas incinerator | |
| CN106524178A (en) | Solid waste incineration cyclone furnace and incineration process for liquid slag of solid waste incineration cyclone furnace | |
| CN206055638U (en) | For the cracking incinerator of waste process of endangering | |
| CN202501481U (en) | Domestic garbage incinerator | |
| CN208487625U (en) | A kind of novel combination type solid-liquid incineration furnace | |
| CN110805911A (en) | Self-discharging type incineration waste ash melting treatment device | |
| CN105889946A (en) | Garbage incinerator | |
| CN105674272B (en) | A kind of compound incinerator of silicon porcelain fire grate and its handling process | |
| CN107178786A (en) | A kind of incinerating method and combinations thereof formula incinerator | |
| CN212227046U (en) | Incinerator for coprocessing solid hazardous waste and liquid hazardous waste | |
| CN2655049Y (en) | Movable grate type solid waste incinerator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | "change of name, title or address" | ||
| CP03 | "change of name, title or address" |
Address after: 300192 Tianjin Binhai New Area Huayuan Industrial Zone Haitai Development Six Road No. 6 Haitai Green Industrial Base G-301-32 Patentee after: XINGHE SPACEFLIGHT TECHNOLOGY (TIANJIN) Co.,Ltd. Address before: 300184 g-301-32, Haitai green industrial base, 6 Haitai development road, Huayuan Industrial Zone, Binhai New Area, Tianjin Patentee before: TIANJIN TENOVIE TECHNOLOGY Co.,Ltd. |