CN106402874A - Garbage incinerator - Google Patents

Garbage incinerator Download PDF

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Publication number
CN106402874A
CN106402874A CN201610666727.2A CN201610666727A CN106402874A CN 106402874 A CN106402874 A CN 106402874A CN 201610666727 A CN201610666727 A CN 201610666727A CN 106402874 A CN106402874 A CN 106402874A
Authority
CN
China
Prior art keywords
secondary air
incinerator
flue
nozzle
jet
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.)
Pending
Application number
CN201610666727.2A
Other languages
Chinese (zh)
Inventor
郭镇宁
韩乃卿
胡建民
刘玉坤
王进
付志臣
张宾
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.)
Everbright Envirotech China Ltd
Everbright Environmental Protection Technology Research Institute Shenzhen Co Ltd
Everbright Environmental Protection Technology Equipment Changzhou Co Ltd
Everbright Environmental Protection China Co Ltd
Original Assignee
Everbright Envirotech China Ltd
Everbright Environmental Protection Technology Research Institute Shenzhen Co Ltd
Everbright Environmental Protection Technology Equipment Changzhou Co Ltd
Everbright Environmental Protection China 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 Everbright Envirotech China Ltd, Everbright Environmental Protection Technology Research Institute Shenzhen Co Ltd, Everbright Environmental Protection Technology Equipment Changzhou Co Ltd, Everbright Environmental Protection China Co Ltd filed Critical Everbright Envirotech China Ltd
Priority to CN201610666727.2A priority Critical patent/CN106402874A/en
Publication of CN106402874A publication Critical patent/CN106402874A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

The invention relates to a garbage incinerator. The garbage incinerator comprises an incinerator grate, an incinerator throat part located above the incinerator grate, and a flue communicating with the incinerator throat part. The incinerator throat part is provided with a plurality of secondary air first nozzles. A plurality of secondary air second nozzles are arranged on the position, above the secondary air first nozzles, of the flue. The secondary air second nozzles and the secondary air first nozzles are both connected to a secondary air mother pipe. The garbage incinerator has the following advantages that 1, through transformation of an air distribution system, the burning capacity of original secondary air nozzles is shared, and thus coking of a hearth is delayed; and 2, the only space of a site is fully used, and the garbage incinerator is suitable for transformation of an aged unit.

Description

A kind of incinerator
Technical field
A kind of the present invention relates to field of waste incineration, in particular it relates to incinerator.
Background technology
During the use of domestic waste incineration row, feed fire grate effect is very crucial, and its reliability directly affects Whole incinerator even entirely burns the reliability of power plant, thus have impact at the house refuse of whole burning power plant Reason ability and economic benefit.
Adopting mechanical garbage incinerator existing waste incineration, the incinerator shown in Fig. 1 is just therein one more Kind.As shown in figure 1, described incinerator include charging aperture 101, feed fire grate 102, be located at burner hearth in for waste incineration Fire grate 103, be located at burn fire grate bottom First air air feed system 104, be located at furnace throat portion Secondary Air air feed system 105 with And slag extractor 106.Additionally, incinerator also includes the flue positioned at described fire grate 103 top, charging aperture 101 front end, it is used for Discharge flue gas.Rubbish pours described incinerator into from charging aperture, is entered by being fed the reciprocating described rubbish of effect of fire grate Enter and burned on the siege in described incinerator, be oven-dried, be dehydrated in rubbish described in described dryer section, described rubbish mainly exists Described burning zone is burnt, and has burnt totally through the rubbish of after-flame section, and remaining slag enters slag extractor afterwards, by arranging Slag machine discharges out of the furnace.Wherein said First air is sent into from the described air compartment burning fire grate bottom, and described Secondary Air is from described rubbish The furnace throat portion of incinerator sends into.
More and more perfect, the calorific value of house refuse with the horizontal more and more higher of domestic and municipal refuse receipts fortune system Also more and more higher therewith, high heating value rubbish burns in incinerator easily makes burner hearth coking, makes burner hearth rear portion tied when serious, blocks up Live the outlet of burner hearth, affect production run;Domestic most incinerator burner hearth mostly is adiabatic furnace, is not provided with burner hearth Water-cooling wall, when refuse thermal value uprises, fire box temperature also increases, and makes coking more serious.
In waste incineration burner hearth, the ash content in rubbish is molten into liquid in thermal-flame or is in soft state, just In the case of often, fire box temperature is maintained at 950 DEG C to 1050 DEG C, if fire box temperature is too high, if ash also maintains soft state When contacting with burner hearth wall, it is easily caused coking, particularly near overfire air jet, due to the volatile matter in rubbish and Secondary Air Produce higher heat after mixing, make that this regional temperature is too high to cause coking.
Separately due to the transformation limited space of incinerator, the size of burner hearth is difficult to change, and cannot arrange water in burner hearth Cold wall.
Accordingly, it would be desirable to improve to described incinerator, to eliminate above-mentioned various problem.
Content of the invention
The present invention provides a kind of incinerator, the stuck problem of effectively solving pusher dolly, makes house refuse simultaneously More uniformly spreading on fire grate, improves combustion efficiency.
The present invention is in order to solve problems of the prior art, there is provided a kind of incinerator, described incinerator bag Include and burn fire grate, be located at the described furnace throat portion burning above fire grate and the flue connecting with described furnace throat portion, in described furnace throat Portion is provided with some Secondary Air first jet, on described flue, is provided with some two above described Secondary Air first jet Secondary wind second nozzle, wherein, described Secondary Air second nozzle and described Secondary Air first jet are connected to Secondary Air main pipe.
Alternatively, it is additionally provided with damper between described Secondary Air second nozzle and described Secondary Air main pipe.
Alternatively, by adjusting the aperture of described damper, to control described Secondary Air second nozzle secondary with described The air quantity of wind first jet.
Alternatively, by adjusting the aperture of described damper, described flue temperature is controlled to be 820 DEG C -880 DEG C
Alternatively, described Secondary Air first jet arranges around described furnace throat portion.
Alternatively, described Secondary Air second nozzle arranges around described flue in the sustained height of described flue.
Alternatively, the distance at the position of described Secondary Air second nozzle to described flue top must assure that the stop of flue gas Time is more than 2 seconds.
Alternatively, it is connected by square pipe between described Secondary Air second nozzle and described Secondary Air main pipe.
Alternatively, described Secondary Air second nozzle and described Secondary Air first jet are all by Secondary Air arm and described two Secondary wind main pipe connection.
Alternatively, the lateral wall of described flue is provided with water-cooling wall, described Secondary Air second nozzle is from described water-cooling wall The gap of wall pipe stretch in described flue.
Alternatively, described Secondary Air second nozzle and described Secondary Air first jet share a blower fan.
Alternatively, described furnace throat portion is adiabatic furnace.
Alternatively, described flue is arranged at the front end of described incinerator.
Incinerator of the present invention has advantages below:
1st, transformed by blowing system, share the quantity combusted of former overfire air jet, the coking of burner hearth can be delayed.
2nd, make full use of live only space it is adaptable to the transformation of old unit.
Brief description
The drawings below of the present invention is used for understanding the present invention in this as the part of the present invention.Shown in the drawings of this Bright embodiment and its description, for explaining assembly of the invention and principle.In the accompanying drawings,
The structure chart of incinerator in Fig. 1 prior art;
Fig. 2 is the structural representation of the incinerator of the present invention;
Fig. 3 is the Secondary Air first jet of incinerator of the present invention and the structural representation of Secondary Air second nozzle.
Accompanying drawing identifies
101st, charging aperture 102, feed fire grate
103rd, fire grate 104, First air air feed system
105th, Secondary Air air feed system 106, slag extractor
1st, hopper chute 2, adiabatic furnace
3rd, water-cooling wall lower header 4, water-cooling wall
5th, secondary first wind nozzle 6, Secondary Air second nozzle
7th, Secondary Air arm 8, Secondary Air main pipe
9th, increased Secondary Air arm
Specific embodiment
In the following description, a large amount of concrete details are given to provide more thorough understanding of the invention.So And, it is obvious to the skilled person that the present invention can one or more of these details and be able to Implement.In other examples, in order to avoid obscuring with the present invention, some technical characteristics well known in the art are not entered Row description.
It should be appreciated that when in this manual using term "comprising" and/or " inclusion ", it indicates that presence is described Feature, entirety, step, operation, element and/or assembly, but do not preclude the presence or addition of other features one or more, entirety, Step, operation, element, assembly and/or combinations thereof.
The present invention is in order to solve problems of the prior art, there is provided a kind of incinerator, as shown in figure 1, tool Body ground include hopper chute 1, adiabatic furnace 2, water-cooling wall lower header 3, water-cooling wall 4, Secondary Air first jet 5, increase secondary Wind first jet 6, Secondary Air arm 7, Secondary Air main pipe 8 and increased Secondary Air arm 9.
Below in conjunction with the accompanying drawings incinerator of the present invention is further described, first described rubbish in the present invention Rubbish incinerator at least includes charging aperture, feed fire grate, the fire grate for waste incineration being located in burner hearth, is located at and burns under fire grate The First air air feed system in portion, the Secondary Air air feed system being located at furnace throat portion and slag extractor.Additionally, incinerator also includes Positioned at the flue of described incinerator front end, for discharging flue gas.Described incinerator can also comprise other conventional parts, Will not be described here.
Reverse-flow incinerator selected by described incinerator in the present invention, wherein reverse-flow incinerator flue setting Front end in incinerator.
Specifically, the furnace throat portion that wherein said incinerator is included above described incinerator is connected with described furnace throat portion Flue, is provided with some Secondary Air first jet in described furnace throat portion, sets on described flue above described overfire air jet It is equipped with some Secondary Air second nozzles, wherein, described Secondary Air second nozzle and described Secondary Air first jet are connected to two Secondary wind main pipe.
Specifically, described Secondary Air first jet arranges around described furnace throat portion, is uniformly arranged at described furnace throat portion.
Alternatively, described Secondary Air second nozzle arranges around described flue in the sustained height of described flue.
Alternatively, it is additionally provided with damper, for adjusting between described Secondary Air second nozzle and described Secondary Air main pipe Save the air quantity of described Secondary Air second nozzle and described Secondary Air first jet, the aperture change institute of big when of for example described damper The air quantity stating Secondary Air second nozzle becomes big, and the air quantity of described Secondary Air first jet diminishes, and the aperture of described damper becomes The air quantity of the described Secondary Air second nozzle of hour diminishes, and the air quantity of described Secondary Air first jet becomes big.
In order to ensure 850 degrees Celsius of 2 seconds rules in the first flue, Secondary Air first jet 6 position of increase to first The distance at flue top must assure that the time of staying of flue gas is more than 2 seconds.
Alternatively, be provided with water-cooling wall on the lateral wall of described flue in the present invention, described Secondary Air second nozzle from The gap of the wall pipe of described water-cooling wall is stretched in described flue.
Because the spacing between water-cooling wall 4 pipe is less, the jet pipe of the Secondary Air first jet 6 of increase adopts square pipe, To make full use of space it is ensured that flow velocity is in scope of design.
For example it is connected by square pipe between described Secondary Air second nozzle and described Secondary Air main pipe.
Wherein, described Secondary Air second nozzle is all secondary with described by Secondary Air arm with described Secondary Air first jet Wind main pipe connects, and by adjusting the aperture of described damper 10, adjusts described Secondary Air second nozzle and described Secondary Air The air quantity of first jet, as shown in Figure 2.
Alternatively, by adjusting the aperture of described damper 10, described flue temperature is controlled to be 820 DEG C -880 DEG C
Preferably, described Secondary Air second nozzle shares a blower fan with described Secondary Air first jet.
As shown in figure 1, the present invention, in the present invention in order to share the quantity combusted of former Secondary Air first jet, delays burner hearth Coking, increases by row's Secondary Air second nozzle 6, Secondary Air second nozzle 6 is from water-cooling wall 4 wall above Secondary Air first jet 5 The flue of boiler is stretched in the gap of pipe, and Secondary Air second nozzle 6 passes through increased Secondary Air arm 5 connecting secondary wind main pipe 8, with Former Secondary Air first jet 5 shares a blower fan, and its air quantity can be adjusted by damper 10.
It is ensured that 100%MCR operating mode secondary air flow is constant during system operation, damper 10 is opened, now Secondary Air One nozzle air quantity reduces, and Secondary Air second nozzle air quantity increases, and the aperture of the situation damper 10 according to slagging, institute State the quantity combusted that Secondary Air second nozzle 6 can share former Secondary Air first jet, the coking of burner hearth can be delayed.
Incinerator of the present invention has advantages below:
1st, transformed by blowing system, share the quantity combusted of former overfire air jet, the coking of burner hearth can be delayed.
2nd, make full use of live only space it is adaptable to the transformation of old unit.
The present invention is illustrated by above-described embodiment, but it is to be understood that, above-described embodiment is only intended to Citing and descriptive purpose, and be not intended to limit the invention in described scope of embodiments.In addition people in the art Member, it is understood that the invention is not limited in above-described embodiment, can also make more kinds of according to the teachings of the present invention Variants and modifications, within these variants and modifications all fall within scope of the present invention.Protection scope of the present invention by The appended claims and its equivalent scope are defined.

Claims (13)

1. a kind of incinerator, described incinerator include burn fire grate, be located at described burn fire grate above furnace throat portion and The flue connecting with described furnace throat portion, is provided with some Secondary Air first jet it is characterised in that described in described furnace throat portion On flue, the top of described Secondary Air first jet be provided with some Secondary Air second nozzles, wherein, described Secondary Air second sprays Mouth and described Secondary Air first jet are connected to Secondary Air main pipe.
2. incinerator according to claim 1 is it is characterised in that described Secondary Air second nozzle and described Secondary Air It is additionally provided with damper between main pipe.
3. incinerator according to claim 2 it is characterised in that by adjust described damper aperture, with Control the air quantity of described Secondary Air second nozzle and described Secondary Air first jet.
4. incinerator according to claim 2 is it is characterised in that by the aperture of the described damper of regulation, control Make described flue temperature and be 820 DEG C -880 DEG C.
5. incinerator according to claim 1 is it is characterised in that described Secondary Air first jet is around described furnace throat Portion arranges.
6. incinerator according to claim 1 is it is characterised in that described Secondary Air second nozzle is in described flue Sustained height arranges around described flue.
7. incinerator according to claim 1 is it is characterised in that the position of described Secondary Air second nozzle is extremely described The distance at flue top must assure that the time of staying of flue gas is more than 2 seconds.
8. incinerator according to claim 1 is it is characterised in that described Secondary Air second nozzle and described Secondary Air Connected by square pipe between main pipe.
9. incinerator according to claim 1 is it is characterised in that described Secondary Air second nozzle and described Secondary Air First jet is all connected with described Secondary Air main pipe by Secondary Air arm.
10. incinerator according to claim 1 is it is characterised in that be provided with water-cooled on the lateral wall of described flue Wall, the gap of the wall pipe from described water-cooling wall for the described Secondary Air second nozzle is stretched into described flue.
11. incinerators according to claim 1 are it is characterised in that described Secondary Air second nozzle is secondary with described Wind first jet shares a blower fan.
12. incinerators according to claim 1 are it is characterised in that described furnace throat portion is adiabatic furnace.
13. incinerators according to claim 1 are it is characterised in that before described flue is arranged at described incinerator End.
CN201610666727.2A 2016-08-12 2016-08-12 Garbage incinerator Pending CN106402874A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610666727.2A CN106402874A (en) 2016-08-12 2016-08-12 Garbage incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610666727.2A CN106402874A (en) 2016-08-12 2016-08-12 Garbage incinerator

Publications (1)

Publication Number Publication Date
CN106402874A true CN106402874A (en) 2017-02-15

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Family Applications (1)

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CN201610666727.2A Pending CN106402874A (en) 2016-08-12 2016-08-12 Garbage incinerator

Country Status (1)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107559831A (en) * 2017-09-01 2018-01-09 佛山市南海绿电再生能源有限公司 A kind of processing method for preventing waste incineration furnace coking
CN108916887A (en) * 2018-09-12 2018-11-30 绿能(杭州)企业管理有限公司 Suppress or eliminate the incinerator primary air arrangement of carbon monoxide
CN109812819A (en) * 2019-03-14 2019-05-28 武汉深能环保新沟垃圾发电有限公司 A kind of garbage burning boiler combustion chamber front and back arch anti-coking system

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008057935A (en) * 2006-09-04 2008-03-13 Mitsubishi Heavy Ind Ltd Stoker type incinerator and its combustion control method
CN202719609U (en) * 2012-05-25 2013-02-06 广州环投技术设备有限公司 Selective air distribution and combustion equipment for garbage incinerator
CN104456577A (en) * 2014-12-03 2015-03-25 重庆三峰卡万塔环境产业有限公司 Hearth of household garbage incinerator based on grate furnace
CN104566389A (en) * 2015-01-16 2015-04-29 光大环保技术装备(常州)有限公司 Low-nitrogen combustion type garbage incinerator and combustion method
CN105371282A (en) * 2015-12-10 2016-03-02 光大环保(中国)有限公司 low-nitrogen combustion garbage incinerator and combustion method
CN205424940U (en) * 2015-12-09 2016-08-03 光大环保(中国)有限公司 Burn burning furnace and overgrate air air distribution equipment suitable for high heating value domestic waste

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008057935A (en) * 2006-09-04 2008-03-13 Mitsubishi Heavy Ind Ltd Stoker type incinerator and its combustion control method
CN202719609U (en) * 2012-05-25 2013-02-06 广州环投技术设备有限公司 Selective air distribution and combustion equipment for garbage incinerator
CN104456577A (en) * 2014-12-03 2015-03-25 重庆三峰卡万塔环境产业有限公司 Hearth of household garbage incinerator based on grate furnace
CN104566389A (en) * 2015-01-16 2015-04-29 光大环保技术装备(常州)有限公司 Low-nitrogen combustion type garbage incinerator and combustion method
CN205424940U (en) * 2015-12-09 2016-08-03 光大环保(中国)有限公司 Burn burning furnace and overgrate air air distribution equipment suitable for high heating value domestic waste
CN105371282A (en) * 2015-12-10 2016-03-02 光大环保(中国)有限公司 low-nitrogen combustion garbage incinerator and combustion method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107559831A (en) * 2017-09-01 2018-01-09 佛山市南海绿电再生能源有限公司 A kind of processing method for preventing waste incineration furnace coking
CN107559831B (en) * 2017-09-01 2018-12-25 佛山市南海绿电再生能源有限公司 A kind of processing method preventing waste incineration furnace coking
CN108916887A (en) * 2018-09-12 2018-11-30 绿能(杭州)企业管理有限公司 Suppress or eliminate the incinerator primary air arrangement of carbon monoxide
CN109812819A (en) * 2019-03-14 2019-05-28 武汉深能环保新沟垃圾发电有限公司 A kind of garbage burning boiler combustion chamber front and back arch anti-coking system

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Application publication date: 20170215