CN206904980U - A kind of refuse incineration system - Google Patents
A kind of refuse incineration system Download PDFInfo
- Publication number
- CN206904980U CN206904980U CN201720632585.8U CN201720632585U CN206904980U CN 206904980 U CN206904980 U CN 206904980U CN 201720632585 U CN201720632585 U CN 201720632585U CN 206904980 U CN206904980 U CN 206904980U
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- China
- Prior art keywords
- incinerators
- flue gas
- incinerator
- incineration system
- refuse incineration
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- 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.)
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Abstract
The utility model provides a kind of refuse incineration system, is related to technical field of waste incineration, solves the technical problem of the high energy consumption of refuse burning system processed in units amount.Refuse burning system includes No.1 incinerator, No. two incinerators, tee pipe fitting and flue gas processing device, the exhanst gas outlet of the No.1 incinerator connects with the first entrance point of the tee pipe fitting, and the exhanst gas outlet of No. two incinerators connects with the second entrance point of the tee pipe fitting;The port of export of the three-way pipe connects with the flue gas processing device, and the flue gas processing device can handle flue gas caused by the No.1 incinerator and No. two incinerators simultaneously.Refuse burning system sets two incinerators, and two incinerators share a set of flue gas processing device, and garbage disposal ability is double so that the energy consumption of processed in units amount reduces, and economic benefit and social benefit are notable.
Description
Technical field
Technical field of waste incineration is the utility model is related to, more particularly, to a kind of refuse incineration system.
Background technology
Burning disposal is that rubbish is placed in incinerator to be burnt, and discharges heat energy, and waste heat recovery can heat supply or generating.
Discharged after gas cleaning, a small amount of residual residue discharge fills or made other purposes.Incineration treatment technology volume reduction is good, innoxious thorough
Bottom, and have energy recovery effect.Therefore, it is the effective of innoxious, minimizing and recycling to carry out house refuse burning disposal
Processing mode.Countries in the world generally use this technology of garbage disposal.
Applicants have discovered that at least there is following technical problem in prior art:
1. the high energy consumption of refuse burning system processed in units amount;
2. the exhaust gas dust content of conventional garbage CIU outlet is high, certain influence is caused on environment.
Utility model content
The purpose of this utility model is to provide a kind of refuse incineration system for setting twin furnace, to solve prior art
Present in refuse burning system processed in units amount high energy consumption technical problem.
To achieve the above object, the utility model provides following technical scheme:
A kind of refuse incineration system provided by the utility model, including No.1 incinerator, No. two incinerators, three-way pipes
Part and flue gas processing device, the exhanst gas outlet of the No.1 incinerator connects with the first entrance point of the tee pipe fitting, described
The exhanst gas outlet of No. two incinerators connects with the second entrance point of the tee pipe fitting;The port of export of the tee pipe fitting with it is described
Flue gas processing device connects, and the flue gas processing device can handle the No.1 incinerator and No. two incinerators production simultaneously
Raw flue gas.
Refuse burning system sets two incinerators, i.e. No.1 incinerator and No. two incinerators, and two incinerators share one
Flue gas processing device is covered, garbage disposal ability is double so that the energy consumption of processed in units amount reduces, and economic benefit and social benefit show
Write.
Further, the No.1 incinerator and No. two incinerators are the straight tubular construction of cylinder.It is straight using cylinder
Cartridge type incinerator, rational in infrastructure, incinerator furnace ventilation is smooth, and oxygen part is abundant, high combustion efficiency;Simple in construction, pad is few,
Incinerator not easy burn-out.
Further, the top surface of the top surface of the No.1 incinerator and No. two incinerators is plane, and two institutes
State and garbage inlet is offered in plane.
The top surface of incinerator is plane, easy to operate, saves manpower.
Further, the flue gas processing device includes spraying dust removal tower, cyclone dust collectors and activated carbon absorption tower, flue gas
Enter the cyclone dust collectors after the spraying dust removal tower dedusting and carry out dedusting, enter back into the activated carbon absorption tower purification.
Further, drying fire grate and combustion furnace are provided with the No.1 incinerator and in No. two incinerators
Row, the drying fire grate and combustion grate are arranged at intervals, and the drying oven is ranked in the top of the combustion grate, the baking
It is preheating and drying area above dry fire grate, is primary zone between the drying fire grate and the combustion grate, the combustion grate
Lower section be burnt zone.
Drying fire grate and combustion grate strengthen the gas permeability of rubbish material, contribute to catching fire and burning for rubbish, burn
Process stabilization.
Further, refuse burning system also includes electrostatic plasma deduster, and the electrostatic plasma deduster is set
Between the cyclone dust collectors and the activated carbon absorption tower.
Electrostatic plasma deduster is introduced into consumer waste incineration system, dust content is greatly lowered, and fume treatment is more
Thoroughly, the purpose that house refuse cleaning is burned is reached.
Further, smoke water separator, the cigarette are additionally provided between the spraying dust removal tower and the cyclone dust collectors
The arrival end of separator is connected by pipeline with the port of export of the spraying dust removal tower, and the port of export of the smoke water separator leads to
The arrival end that pipeline is crossed with the cyclone dust collectors connects.
Further, rapidly rubbish is poured into incinerator for convenience, refuse burning system also includes dumping
Platform, the dumping platform are on a horizontal plane with the burning furnace top surface.
Further, refuse burning system also includes waste water treatment device, and the waste water treatment device removes with the spray
The slag-drip opening connection of the bottom of chimney.
Buck caused by refuse burning system is focused on, reduces the influence to environment.
Further, the waste water treatment device includes sedimentation basin.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, drawings in the following description are only
It is some embodiments of the utility model, for those of ordinary skill in the art, is not paying the premise of creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is a kind of schematic top plan view of the layout of refuse incineration system of the utility model;
Fig. 2 is the structural representation of one embodiment of the present utility model.
1- No.1s incinerator in figure;11- dries fire grate;12- combustion grates;No. bis- incinerators of 2-;3- tee pipe fittings;41-
Spraying dust removal tower;42- cyclone dust collectors;43- activated carbon absorption towers;44- electrostatic plasma dedusters;45- smoke water separators;5-
Garbage inlet;6- dumping platforms;7- centrifugal blowers, 8- chimneys.
Embodiment
, below will be to technology of the present utility model to make the purpose of this utility model, technical scheme and advantage clearer
Scheme is described in detail.Obviously, described embodiment is only the utility model part of the embodiment, rather than all
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not before creative work is made
Resulting all other embodiment is put, belongs to the scope that the utility model is protected.
As depicted in figs. 1 and 2, the utility model provides a kind of refuse incineration system, including No.1 incinerator 1,
No. two incinerators 2, tee pipe fitting 3 and flue gas processing device, the exhanst gas outlet of the No.1 incinerator 1 and the tee pipe fitting 3
The connection of the first entrance point, the exhanst gas outlet of No. two incinerators 2 connects with the second entrance point of the tee pipe fitting 3;Institute
The port of export for stating tee pipe fitting 3 connects with the flue gas processing device, and the flue gas processing device can handle described one simultaneously
Flue gas caused by number incinerator 1 and No. two incinerators 2.
Refuse burning system sets two incinerators, i.e. No.1 incinerator 1 and No. two incinerators 2, two incinerators share
A set of flue gas processing device, garbage disposal ability are double so that the energy consumption of processed in units amount reduces, economic benefit and social benefit
Significantly.
For example, the power consumption during refuse burning system of the single stove 4 tons of rubbish of processing in one day is 4 degree/h, it is latter to be changed to twin furnace
Power consumption during its 8 tons of rubbish of processing is 6 degree/h, and the energy consumption of processed in units amount reduces.
Garbage transporting artificial simple classification to after burning place enters No.1 incinerator 1 and No. two incinerators 2, incineration firing
The flow path of caused flue gas is afterwards:Spraying dust removal tower 41 → again cool down 45 → cyclone dust collectors of smoke adding separator 42 →
43 → chimney of electrostatic plasma deduster 44 → centrifugal blower, 7 → activated carbon absorption tower 8.
Optionally embodiment, No.1 incinerator 1 and No. two incinerators 2 use circular flat mouth feed design, rubbish
Rubbish enters stove and enters body conveniently, and operating personnel are light, and incinerator designs the needs that can meet all weather operations, continuously-running and interruption
Operation, year run time be not less than 8000 hours, projected life be more than 8 years.Furnace body shell is steel construction, and inwall is dissimilarity
The fire resisting cast material of matter, internal layer are high temperature resistant casting material, are resistant to 1200 DEG C of high temperature, centre is lightweight refracrory, both may be used
There are enough ignition temperatures in guarantee, shell low temperature can be kept again, with anti-scald, refractory material is integral cast, difficult for drop-off,
It is not perishable.The ton day of equipment day output 2 to 50.
Water makes dusty gas fully be connect with fluid by nozzle atomisation or by column plate in spraying dust removal tower 41
Touch, collision, interception and cohesion between grit and drop, under grit lands with drop.This deduster simple structure, resistance
Power is smaller, it is easy to operate, the higher gas of dust content can be handled blocked without causing.Spray beautiful jade formula deduster can use
Recirculated water, untill particulate matter in washing lotion reaches at a relatively high degree, so as to enormously simplify water processing establishment.So this
Kind deduster still has many enterprises to use so far.Its advantages of is that equipment volume is smaller, and water can precipitate Posterior circle use.Need
Want the technique that pressure is high, reaches cooling.
Electrostatic plasma cleaner is popular to say using electric charge field and the method for separating electric field unification:Use highfield
Make charge dust particles, when it passes through electrodes for removing dust, the particulate with positive/negative electric charge is adsorbed by positive negative battery lead plate respectively, that is, reaches
When to dedusting purpose its operation principles being flue gas by flue before electrostatic precipitator main structure, make its flue dust positively charged,
Then flue gas enters the electrostatic precipitator channel for setting multi-layer cathode plate.Due to the mutual absorption of positively charged flue dust and cathode electric board
Effect, the particle dust in flue gas is set to adsorb on negative electrode, minus plate is hit in timing, makes that there is certain thickness flue dust to conduct oneself with dignity
With fall under the double action of vibration in ash bucket below electrostatic precipitator structure, so as to reach flue dust and the combustion removed in flue gas
Plastic products produce oily nuisance, electrostatic 220 volts of plasma smoke abatement cleaner working voltage in burning, and power consumption is
0.2kw, equipment and technology is ripe for many years, periodic cleaning ash bucket dirt oil, convenient and simple operation, and being adapted to villages and towns in rural areas to burn field makes
With.
Cyclone dust collectors 42 are dust-contained airflow is made high speed rotary motion, by the effect of centrifugal force by particulate matter from air-flow
It is middle to separate and collect the dust arrester to get off.Decline into the dust-contained airflow of cyclone dust collectors 42 along simplified inwall in rotation,
Have that a small amount of gas is radially movable into central area simultaneously, when swirling eddy most of is reached near cone base, then
Start to switch to move upwards, central area rises in rotation, is finally discharged by outlet, while there is also the radial direction of centrifugation
Motion.Downward outer ring air-flow will generally be rotated and be referred to as outer vortex, and the region of cone base is called recirculating zone or mixed flow
Area.
Contained particulate matters progressively settle under the influence of centrifugal force in rotary movement in the flue gas of cyclone dust collectors 42
Grow sturdily on the inwall for applying dirt device, and under the promotion of outer vortex and Action of Gravity Field, most of particulate matter gradually lands along cone inwall
Into ash bucket.In addition, the small part air-flow in inlet air flow rotates upward, after top end cover and continuation edge in arrival along simplified inwall
Export pipe outer wall rotation to decline, finally reach the air-flow that outlet lower end is raised and take away.Generally this fraction is claimed
For upper vortex.With upper vortex, there will be a small amount of fine particle to be taken away upwards by interior vortex.Equally, also there is few portion in mixed flow region
Divide fine particle to be taken up upwards by interior vortex, and partly taken away.Cyclone dust collectors 42 are exactly to complete particle through the above way
The trapping of thing.The particulate matter trapped is located in the ash bucket of deduster bottom, from deduster discharge can be still contained in gas
Part tiny particles content.
The form of cyclone dust collectors 42 is more, different in the way of air-flow enters, and can be roughly divided into and tangentially enter and axially enter
Enter two major classes.Promote flow rotation by guide vane axially into formula, therefore also make guide vane rotary.Axially into
Formula can be divided into reverse-flow and single flow again.Tangential entry type is divided into the forms such as straight people's formula and scroll casing type again:The inlet tube of straight people's formula
Outer wall is tangent with cylinder;And the entrance inside pipe wall and cylinder of scroll casing type are tangent.My company removes using tangential direct-insert whirlwind
Dirt device 42.
Cyclone dust collectors 42 are applied to non-sticky of the purification more than 1-3 microns, the dried dust of non-fiber.It is a kind of knot
Structure is simple and convenient to operate, the cleaning equipment of high temperature resistant, cost of equipment and resistance higher (80~160 millimeter of water), cyclone dust removal
Device 42 is applied the most extensive in cleaning equipment.
In incineration firing smoke exhaust process, active carbon filtration sandwich layer is mounted with charcoal absorption tower, be it is a kind of by
Outward appearance made of carbonaceous material is in black, and internal pore structure is flourishing, specific surface area is big, a kind of microcrystalline carbon of adsorption capacity by force
Cellulosic material.There are a large amount of invisible micropores in absorbent charcoal material, total internal surface area of micropore can be high in 1 gram of absorbent charcoal material
Up to 700~2300 square metres, that is to say, that in the activated carbon granule of a grain of rice size, the internal surface area of micropore equivalent to
The size of one stateroom inner wall surface.Exactly these micropores enable the various toxic and harmful gas of activated carbon " seizure " and impurity.
Activated carbon suction tower has played key decomposition flue gas in garbage incinerating system, when activated carbon molecule and pernicious gas contact,
Physical absorption adsorption strength it is mainly relevant with the physical property of activated carbon.Because Van der Waals force is weaker, to contaminant molecule
Structure influence little, physical absorption can be analogized to coacervation by this power as intermolecular cohesion.Physical absorption
When pollutant chemical property remain in that it is constant.
Because chemical bond is strong, the structure of contaminant molecule is had a great influence, therefore chemisorbed can be regarded as chemical reaction, is
The result of chemical action between pollutant and activated carbon.Chemisorbed generally comprises electronics and shared or electronics is shifted, rather than letter
Single perturbation or weak polarization, are irreversible chemical reaction processes.Adsorption process is that contaminant molecule is adsorbed to solid
The process on surface, the free energy of molecule can reduce, and therefore, adsorption process is exothermic process, and the heat released is referred to as the pollutant
Heat of adsorption on this surface of solids.Because physical absorption is different with the active force of chemisorbed, they are in heat of adsorption, absorption speed
Rate, activation energy of adsorption, adsorption temp, selectivity, the absorption number of plies and absorbance spectrum etc. show certain difference.
Active carbon adsorption technology is used for purification of air at home, medicine, and the refined and decolouring of the industry such as chemical industry and food is
There is history for many years.Start the seventies to be used for Industrial Wastewater Treatment.Production practices show that activated carbon is to trace toxic gas in flue gas
Adsorptivity with brilliance, it has good to industrial wastewaters such as textile printing and dyeing, dye chemical industry, food processing and organic chemical industries
Adsorption effect.Generally, to the organic matter represented in cigarette with overall targets such as BOD, COD, such as conbustion synthesis dyestuff, surface
Property agent, phenols, benzene class, organochlorine, fired in plastic products etc., have the removal ability of uniqueness.So active carbon adsorption is
Progressively turn into one of incineration treatment of garbage discharge main method.
It is described above, only specific embodiment of the present utility model, but the scope of protection of the utility model is not limited to
In this, any one skilled in the art can readily occur in change in the technical scope that the utility model discloses
Or replace, it should all cover within the scope of protection of the utility model.Therefore, the scope of protection of the utility model should be with the power
The protection domain that profit requires is defined.
Claims (10)
1. a kind of refuse incineration system, it is characterised in that including No.1 incinerator (1), No. two incinerators (2), three-way pipes
Part (3) and flue gas processing device, the exhanst gas outlet of the No.1 incinerator (1) and the first entrance point of the tee pipe fitting (3)
Connection, the exhanst gas outlet of No. two incinerators (2) connect with the second entrance point of the tee pipe fitting (3);The three-way pipe
The port of export of part (3) connects with the flue gas processing device, and the flue gas processing device can handle the No.1 simultaneously and burn
Flue gas caused by stove (1) and No. two incinerators (2).
A kind of 2. refuse incineration system according to claim 1, it is characterised in that the No.1 incinerator (1) and
No. two incinerators (2) are the straight tubular construction of cylinder.
3. a kind of refuse incineration system according to claim 2, it is characterised in that the No.1 incinerator (1)
Top surface and the top surface of No. two incinerators (2) are plane, and garbage inlet (5) is offered in two planes.
4. a kind of refuse incineration system according to claim 1, it is characterised in that the flue gas processing device includes
Spraying dust removal tower (41), cyclone dust collectors (42) and activated carbon absorption tower (43), flue gas is in the spraying dust removal tower (41) dedusting
Enter the cyclone dust collectors (42) afterwards and carry out dedusting, enter back into the activated carbon absorption tower (43) and purified.
5. a kind of refuse incineration system according to claim 4, it is characterised in that in the No.1 incinerator and institute
State and drying fire grate (11) and combustion grate (12) are provided with No. two incinerators, the drying fire grate (11) and the combustion furnace
Arrange (12) to be arranged at intervals, and the drying fire grate (11) is located at the top of the combustion grate (12), the drying fire grate (11)
Top be preheating and drying area, it is described drying fire grate (11) and the combustion grate (12) between be primary zone, the combustion furnace
It is burnt zone to arrange below (12).
6. a kind of refuse incineration system according to claim 4 or 5, it is characterised in that also including electrostatic plasma
Deduster (44), the electrostatic plasma deduster (44) are arranged at the cyclone dust collectors (42) and the activated carbon absorption tower
(43) between.
A kind of 7. refuse incineration system according to claim 6, it is characterised in that the spraying dust removal tower (41) and
Smoke water separator (45) is additionally provided between the cyclone dust collectors (42), the arrival end of the smoke water separator (45) passes through pipe
Road connects with the port of export of the spraying dust removal tower (41), and the port of export of the smoke water separator (45) passes through pipeline and the rotation
The arrival end connection of wind deduster (42).
8. a kind of refuse incineration system according to claim 7, it is characterised in that also including dumping platform
(6), the dumping platform (6) is in one with the top surface of the No.1 incinerator and the top surface of No. two incinerators
On horizontal plane.
A kind of 9. refuse incineration system according to claim 8, it is characterised in that also including waste water treatment device,
The waste water treatment device connects with the slag-drip opening of the bottom of the spraying dust removal tower (41).
A kind of 10. refuse incineration system according to claim 9, it is characterised in that the waste water treatment device bag
Include sedimentation basin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720632585.8U CN206904980U (en) | 2017-06-02 | 2017-06-02 | A kind of refuse incineration system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720632585.8U CN206904980U (en) | 2017-06-02 | 2017-06-02 | A kind of refuse incineration system |
Publications (1)
Publication Number | Publication Date |
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CN206904980U true CN206904980U (en) | 2018-01-19 |
Family
ID=61286010
Family Applications (1)
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CN201720632585.8U Expired - Fee Related CN206904980U (en) | 2017-06-02 | 2017-06-02 | A kind of refuse incineration system |
Country Status (1)
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CN (1) | CN206904980U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109373331A (en) * | 2018-11-28 | 2019-02-22 | 钟天路 | A kind of full-automatic waste incinerator of high-effective dust-removing and its process |
-
2017
- 2017-06-02 CN CN201720632585.8U patent/CN206904980U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109373331A (en) * | 2018-11-28 | 2019-02-22 | 钟天路 | A kind of full-automatic waste incinerator of high-effective dust-removing and its process |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180119 Termination date: 20200602 |