CN209672350U - A kind of burning processing system - Google Patents
A kind of burning processing system Download PDFInfo
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- CN209672350U CN209672350U CN201822167532.0U CN201822167532U CN209672350U CN 209672350 U CN209672350 U CN 209672350U CN 201822167532 U CN201822167532 U CN 201822167532U CN 209672350 U CN209672350 U CN 209672350U
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- incinerator
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- burning processing
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- 239000002699 waste material Substances 0.000 claims abstract description 40
- 239000007789 gas Substances 0.000 claims abstract description 13
- 239000007921 spray Substances 0.000 claims description 34
- 239000010721 machine oil Substances 0.000 claims description 30
- 238000007789 sealing Methods 0.000 claims description 23
- 239000004568 cement Substances 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 14
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 6
- 239000010913 used oil Substances 0.000 claims description 5
- 238000000354 decomposition reaction Methods 0.000 claims description 4
- 238000010586 diagram Methods 0.000 description 10
- 239000002910 solid waste Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 230000008901 benefit Effects 0.000 description 7
- 239000003973 paint Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 241000251468 Actinopterygii Species 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000010920 waste tyre Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000036244 malformation Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
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- 238000006467 substitution reaction Methods 0.000 description 1
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- 230000002195 synergetic effect Effects 0.000 description 1
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The utility model embodiment discloses a kind of burning processing system.The burning processing system includes: rotary incinerator, the burning disposal for waste；Dore furnace is connected with the rotary incinerator, the processing of the burning gases for obtaining after castoff burning processing；Tertiary-air pipe is connected with the rotary incinerator, for being passed through high-temperature gas into the rotary incinerator；And the tertiary-air pipe is connected to the side of the rotary incinerator, the hull outside of the tertiary-air pipe and the shell of the rotary incinerator are tangent.In the burning processing system, rotary incinerator and tertiary-air pipe and dore furnace are closely combined into an organic whole, constitute online castoff burning processing system, realize difficulty set, innoxious, the disposal of resources of the wastes such as nonflammable industrial refuse.
Description
Technical field
The utility model relates to garbage decomposition technical field, in particular to a kind of burning processing system.
Background technique
Currently the precombustion of solid waste is handled mostly based on fire grate, main problem existing for this processing mode
It is that grate failure rate is high, and there are also the residue cokings after glass and metal burning to be not easy to be discharged in solid waste.Upper
Century, the eighties just had attempted to using rotary pre- burner to the processing of solid waste precombustion.
The main body of cement kiln synergic processing waste is to rely on cement kiln, if directly put into solid waste at rotary kiln incineration
Comprehend and cause very big influence to the stability of rotary kiln operating condition, and in rotary kiln some solid wastes (as paint slag, small paint can,
Waste tire) nonflammable processing.Solid waste first pretreatment before investment rotary kiln incineration processing will improve revolution
Kiln can reduce the influence to rotary kiln to the treating capacity of solid waste.
In view of the above-mentioned problems, expecting there is a kind of new burning processing system.
Utility model content
In view of the above problems, the purpose of this utility model is to provide a kind of burning processing systems, to realize difficulty
It sets, innoxious, the disposal of resources of the wastes such as nonflammable industrial refuse, and realizes waste treatment and waste.
One side according to the present utility model provides a kind of burning processing system, comprising:
Rotary incinerator, the burning disposal for waste；
Dore furnace is connected with the rotary incinerator, the combustion gas for obtaining after castoff burning processing
The processing of body；
Tertiary-air pipe is connected with the rotary incinerator, for being passed through High Temperature Gas into the rotary incinerator
Body；And
The tertiary-air pipe is connected to the side of the rotary incinerator, the hull outside of the tertiary-air pipe with it is described
The shell of rotary incinerator is tangent.
Preferably, the burning processing system further include:
First machine oil spray gun, positioned at the interface of the tertiary-air pipe and the rotary incinerator, for the height
The heating of wet body；
Second machine oil spray gun, positioned at the top of the rotary incinerator, for improving the furnace of the rotary incinerator
Interior temperature；
Third machine oil spray gun, positioned at the top of the rotary incinerator, the straight section position of the dore furnace, described in
In dore furnace, for maintaining the in-furnace temperature of the dore furnace.
Preferably, the first machine oil spray gun, the second machine oil spray gun, the third machine oil spray gun spray material be
Used oil.
Preferably, the dore furnace includes two sections, and the upper section of the dore furnace is straight section, the lower section of the dore furnace
For cone cell；And
The rotary incinerator is connected with the straight part of the dore furnace.
Preferably, the burning processing system is at least further include:
Feed lines are connected with the rotary incinerator, the addition for the waste；
First blanking air valve is located in the feed lines, for controlling the feeding capacity of the waste；
Second blanking air valve is located in the feed lines, for controlling the feeding capacity of the waste.
Preferably, the burning processing system further include:
Buffer unit is located in the feed lines, rushes for reducing the waste to the rotary incinerator
It hits；And
The buffer unit includes being selected from least one of beam type, chain type, grid type.
Preferably, the rotary incinerator includes:
Incinerator turntable, positioned at the bottom of the rotary incinerator, the rotation of waste described in the incinerator driven by rotary disc
Turn；
Fixed baffle is located in the rotary incinerator, treated for being discharged waste combustion residue.
Preferably, the burning processing system further include:
Cement kiln, the cement kiln are located at the lower section of the rotary incinerator and the dore furnace, the cement kiln
It is connected with the dore furnace；And
The waste combustion treated the residue is discharged by the rotary incinerator, by the dore furnace,
It falls into the cement kiln.
Preferably, the incinerator turntable and the rotary sealing burned between furnace shell are using flap sealing shape
Formula.
The embodiments of the present invention have the following advantages that or the utility model has the advantages that rotary incinerator and tertiary-air pipe and decomposition
Furnace is closely combined into an organic whole, merges among quality coal in cement kiln systems, to constitute online castoff burning processing
System does not have cold air injection in entire burning processing system, hot-oil circulation is not necessarily to, without exhaust gas and residue outlet, heat loss
Seldom, secondary pollution will not be caused, realize difficulty set, innoxious, the disposal of resources of the solids such as nonflammable industrial refuse.
The embodiments of the present invention have the following advantages that or the utility model has the advantages that include used oil spray in burning processing system
Rifle can guarantee rotary burning in-furnace temperature, stablize calciner temperature, and can dispose useless while disposing waste
Machine oil realizes waste recycling.
The embodiments of the present invention have the following advantages that or the utility model has the advantages that rotary burning stove outer covering and tertiary air shell
The connection of body is in tangent line form, and hot wind is entered in incinerator by tertiary-air pipe, and hot wind rotates in incinerator along shell camber line,
It enters back into dore furnace, while reducing wind resistance three times, comes into full contact with tertiary air with solid waste, improve burning effect
Rate.
Detailed description of the invention
By referring to the drawings to the description of the utility model embodiment, above-mentioned and other mesh of the utility model
, feature and advantage will be apparent from, in the accompanying drawings:
Fig. 1 shows the structural schematic diagram of the burning processing system according to the utility model embodiment；
Fig. 2 shows the structural schematic diagrams according to the rotary incinerator of the utility model embodiment:
Fig. 3 shows the partial schematic diagram of the burning processing system according to the utility model embodiment；
Fig. 4 shows the structural schematic diagram sealed according to the incinerator of the burning processing system of the utility model embodiment；
Fig. 5 shows the structural schematic diagram of the burning processing system according to the utility model embodiment.
Specific embodiment
Hereinafter reference will be made to the drawings is more fully described the various embodiments of the utility model.In various figures, identical
Element is indicated using same or similar appended drawing reference.For the sake of clarity, the various pieces in attached drawing are not drawn to draw
System.In addition, certain well known parts may be not shown in figure.
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Under
Described in the text many specific details of the utility model, such as structure, material, size, treatment process and the technology of component,
To be more clearly understood that the utility model.But it just as the skilled person will understand, can not be according to this
Some specific details realize the utility model.
It should be appreciated that being known as being located at another floor, another area when by a floor, a region when describing the structure of component
When domain " above " or " top ", can refer to above another layer, another region, or its with another layer, it is another
Also comprising other layers or region between a region.Also, if by part turnover, this layer, a region will be located at it is another
Layer, another region " following " or " lower section ".
Fig. 1 shows the structural schematic diagram of the burning processing system according to the utility model embodiment.As shown in Figure 1, burning
Burning processing system includes incinerator conveying device 10, the hydraulic blanking air valve 20 of the first incinerator, the hydraulic blanking of the second incinerator
The hydraulic blanking air valve 40 of air valve 30, third incinerator, rotary incinerator 50, dore furnace 60, tertiary-air pipe 70, cement kiln
80, the first machine oil spray gun 91, the second machine oil spray gun 92, third machine oil spray gun 93.Various difficulty set danger wastes can individually or
Person, which mixes to be packaged, is sent into burning processing system by incinerator conveying device 10.The danger wastes that can be disposed include: paint slag, small
The high heating values such as paint can, waste tire, cloth, plastics, difficulty set hazardous waste.Waste successively pass through the first incinerator it is hydraulic under
Material air valve 20, the hydraulic blanking air valve 30 of the second incinerator, the hydraulic blanking air valve 40 of third incinerator are sent into rotary burn
Burn furnace 50.It between incinerator conveying device 10 and rotary incinerator 50, is connected by pipeline, the first burning is provided on pipeline
The hydraulic blanking air valve 20 of furnace, the hydraulic blanking air valve 30 of the second incinerator, the hydraulic blanking air valve 40 of third incinerator and
Buffer unit.Buffer unit is for reducing impact of the waste to rotary incinerator 50.Buffer unit can be beam type, chain type
Or grid type.Rotary incinerator 50 is connected with tertiary-air pipe 70.Rotary incinerator 50 and 70 shell of tertiary-air pipe
Connection is in tangent line form, and hot wind enters rotary incinerator 50 by tertiary-air pipe 70.Rotary incinerator 50 has rotatable
Component, and revolving speed is adjustable.The burning of waste is carried out in rotary incinerator 50.The upper end of rotary incinerator 50 and decomposition
The straight section of furnace 60 is connected directly.The burning gases generated in rotary incinerator 50 fully enter in dore furnace 60 at burning
Reason.Relatively coarse grain residue in rotary incinerator 50 after trash burning is fallen into cement kiln 80 by dore furnace 60, participates in water
The firing of mud clinker is reacted.Dore furnace 60 can be divided into two sections from top to bottom, and top is straight part, and straight part is taper below
Part.In the burning processing system of the utility model embodiment, further include the first machine oil spray gun 91, the second machine oil spray gun 92,
Third machine oil spray gun 93.First machine oil spray gun 91 is located at the interface of tertiary-air pipe 70 Yu rotary incinerator 50, for heating
Tertiary air.Second machine oil spray gun 92 is located at turn around the top of formula incinerator 50, for improving the temperature in rotary incinerator 50.
Third machine oil spray gun 93 is located at turn around the top of formula incinerator 50, and the straight section position of dore furnace 60 is used for towards in dore furnace 60
Guarantee the temperature in dore furnace 60.
In the above-described embodiments, rotary incinerator, dore furnace and tertiary-air pipe are closely linked, and form online
Waste cooperative disposal system.Hot gas, the residue that incinerator internal combustion bakes useless generation enter dore furnace.Entire burning processing system
In there is no cold air injection, be not necessarily to hot-oil circulation, without exhaust gas and residue outlet, heat loss is few, will not cause secondary dirt
Dye.While realizing environmental protection, reduce costs.
In one embodiment of the utility model, when burning processing system is in close state, the first incinerator liquid
Pressure material air valve 20, the hydraulic blanking air valve 30 of the second incinerator, the hydraulic blanking air valve 40 of third incinerator are in pass
Closed state.When burning processing system is in operating status, the hydraulic blanking air valve 20 of the first incinerator, the second incinerator are hydraulic
At least one in the hydraulic blanking air valve 40 of blanking air valve 30, third incinerator is in close state, to reduce at burning
Reason system is leaked out.By adjusting the hydraulic blanking air valve 20 of the first incinerator, the hydraulic blanking air valve 30 of the second incinerator, the
The folding of the hydraulic blanking air valve 40 of three incinerators controls the waste feed quantity to rotary incinerator 50, to control back
Temperature in rotary incinerator 50.
In the above-described embodiments, the feed quantity of waste is controlled by three valves.Operation is in burning processing system
When state, guarantees that at least one valve is in close state, reduce the heat loss of burning processing system.
In one embodiment of the utility model, burning processing system includes the first machine oil spray gun 91, the second machine oil
Spray gun 92, third machine oil spray gun 93, are located at the different location of burning processing system, are respectively used to guarantee tertiary air, revolution
The temperature of formula incinerator 50 and dore furnace 60.First machine oil spray gun 91, the second machine oil spray gun 92, third machine oil spray gun 93 can be with
It is used cooperatively according to the practical operation situation of burning processing system, to guarantee the temperature of different parts.The machine that machine oil spray gun sprays
Oil can be used oil.
In the above-described embodiments, machine oil spray gun is set in different positions, the temperature to burning processing system may be implemented
Control.Fuel of the used oil as substitution can be used in machine oil spray gun, can reduce the coal consumption of clinker, realizes with useless system
It is useless.
In one embodiment of the invention, wind-warm syndrome when burning processing system is in operating status, in tertiary-air pipe 70
It is kept for 700-900 DEG C, is tertiary air heating by grate-cooler；Temperature in dore furnace 60 is remained above 840 DEG C；Always revolution is maintained
Fuel gas temperature in formula incinerator 50 is 800-1000 DEG C.By adjusting the revolving speed of rotating device in rotary incinerator 50, make
Waste just full combustion in 5-30 minutes time in rotary incinerator 50.
Fig. 2 shows the structural schematic diagrams according to the rotary incinerator of the utility model embodiment.As shown in Fig. 2, returning
Rotary incinerator 50 includes burning furnace shell castable 5001, burning furnace shell 5002, incinerator turntable castable 5003, burn
Furnace turntable 5004, incinerator turntable lacing film 5005, incinerator seal 5006, incinerator bearing upper bracket 5007, incinerator center
Column 5008, tertiary air entrance 5009, incinerator bearing upper bracket 5010, incinerator slewing bearing 5011, incinerator bearing
Undersetting 5012.Burning furnace shell castable 5001 is a kind of thermal insulation material, is located at and burns in furnace shell 5002, for rotary
The heat preservation of incinerator 50.The peripheral side that furnace shell 5002 is located at turn around formula incinerator 50 is burned, for protecting rotary incinerator
50.Incinerator turntable 5004 is located at turn around the bottom of formula incinerator 50, and incinerator turntable 5004 can rotate, and revolving speed can
It adjusts.Incinerator turntable 5004 carries waste rotation, keeps the burning disposal of waste more abundant.Incinerator turntable castable
5003 are located in incinerator turntable 5004, the heat preservation for rotary incinerator 50.Incinerator turntable lacing film 5005, which is located at, to be burned
The peripheral side of furnace turntable castable 5003 and incinerator turntable 5004 prevents high temperature from making turntable steel for guaranteeing the stabilization of structure
Malformation.Incinerator sealing 5006 is used for the sealing of rotary incinerator 50.Incinerator bearing upper bracket 5007 is located at turn around
The top of formula incinerator 50 is used to support incinerator newel 5008.Incinerator newel 5008 is incinerator turntable 5004
Rotation center, longitudinally through entire rotary incinerator 50, for guaranteeing the stability of structure.Tertiary air entrance 5009 is located at back
On the side wall of rotary incinerator 50, it is connected with tertiary-air pipe 70, the importing for tertiary air.Incinerator bearing undersetting 5010
In the bottom of rotary incinerator 50, it is used to support incinerator newel 5008.Incinerator slewing bearing 5011, which is located at, to be burnt
The bottom for burning furnace newel 5008, friction when being used to support incinerator newel 5008 and reducing rotation.Incinerator bearing
Seat 5012 is located at the bottom of incinerator slewing bearing 5011, is used to support incinerator slewing bearing 5011.
It is resistance in the disk peripheral installation 06Cr25Ni20 of rotary incinerator 50 in one embodiment of the utility model
Hot steel lacing film prevents high temperature from deform turntable steel construction, influences rotary incinerator 50 and runs well.
Fig. 3 shows the partial schematic diagram of the burning processing system according to the utility model embodiment.As shown in figure 3, burning
The part for burning processing system includes dore furnace 60, tertiary-air pipe 70, fixed baffle 5013, material inlet 5014.It is rotary to burn
It burns the burning gases generated in furnace 50 and fully enters burning processing in dore furnace 60.Relatively coarse grain inorganic residues after waste combustion are logical
It crosses under 5004 rotating force of fixed baffle 5013 and incinerator turntable and incineration residue is discharged into dore furnace 60.Material inlet 5014
It is located at turn around the top of formula incinerator, is connected by pipeline with incinerator conveying device 10, the importing for material.It is rotary to burn
The connection for burning 50 shell of furnace and 70 shell of tertiary-air pipe is in tangent line form, and hot wind enters rotary incinerator by tertiary-air pipe 70
It rotates, enters back into dore furnace 60 in rotary incinerator 50 along shell camber line in 50.
In the above-described embodiments, the rotary stove outer covering and the connection of tertiary-air pipe shell of burning is in tangent line form, and hot wind is logical
It crosses after tertiary-air pipe enters incinerator, hot wind rotates in incinerator along shell camber line, enters back into dore furnace.It is reduced realizing
It three times while wind resistance, comes into full contact with tertiary air with solid waste, improves efficiency of combustion.
Fig. 4 shows the structural schematic diagram sealed according to the incinerator of the burning processing system of the utility model embodiment.
As shown in figure 4, the incinerator sealing 5006 of the burning processing system includes first sealing device 5021, composite plate 5022, fish scale
Piece 5023, the second sealing device 5024.Incinerator sealing 5006 is located at turn around on formula incinerator 50, is used for incinerator turntable
5004 with burn furnace shell 5002 sealing.First sealing device 5021 is located at the outermost of sealing position, for sealing.It is compound
Plate 5022 is connected with first sealing device 5021, positioned at the inside of first sealing device 5021.Flap 5023 and composite plate
5022 are connected, and positioned at the inside of composite plate 5022, constitute flap sealing.Second sealing device 5024 and 5023 phase of flap
Connection, positioned at the inside of flap 5023, for sealing.
In the above-described embodiments, the sealing of the incinerator turntable of rotary incinerator and burning furnace shell includes using fish scale
The sealing means of piece sealing, sealing effect are more more preferable than tradition machinery sealing effect.
Fig. 5 shows the structural schematic diagram of the burning processing system according to the utility model embodiment.As shown in figure 5, showing
Each device in burning processing system, the connection between each device and the conveying of the material between each device are gone out.It is useless
Gurry (material) is added in burning processing system by incinerator conveying device 10.Waste successively passes through three feeding valves 21
It is fed through in rotary incinerator 50 with blanking buffer device 22.Three feeding valves 21 are used to control the additive amount of waste, under
Material buffer unit 22 is for reducing impact of the material to rotary incinerator 50.Rotary incinerator 50 burn after gas and compared with
Coarse grain residue enters in dore furnace 60.Gas passes through the uptake flue of dore furnace 60, into the first raw material silo 25 and the second raw material
Storehouse 24.It compared with the uptake flue that coarse grain residue passes through dore furnace 60, falls into smoke-box 23, and then enters in cement kiln 80.First is raw
Feed bin 25 into smoke-box 23 for adding materials.Second raw material silo 24 into dore furnace 60 for adding materials.The burning disposal
System further includes grate-cooler 26, and grate-cooler 26 is for providing and heating tertiary air.The tertiary air that grate-cooler 26 provides respectively enters
In rotary incinerator 50 and in dore furnace 60.
In the above-described embodiments, it is provided with buffer unit in the conveying device of waste, reduces waste to incinerator
The impact of turntable ensure that the reliability of device.
It should be noted that herein, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that
There is also other identical elements in process, method, article or equipment including the element.
It is as described above according to the embodiments of the present invention, these embodiments details all there is no detailed descriptionthe,
Also not limiting the utility model is only the specific embodiment.Obviously, as described above, many modification and change can be made
Change.These embodiments are chosen and specifically described to this specification, is in order to preferably explain the principles of the present invention and actually to answer
With so that skilled artisan be enable to utilize the utility model and repairing on the basis of the utility model well
Change use.The utility model is limited only by the claims and their full scope and equivalents.
Claims (9)
1. a kind of burning processing system characterized by comprising
Rotary incinerator, the burning disposal for waste；
Dore furnace is connected with the rotary incinerator, the burning gases for obtaining after castoff burning processing
Processing；
Tertiary-air pipe is connected with the rotary incinerator, for being passed through high-temperature gas into the rotary incinerator；With
And
The tertiary-air pipe is connected to the side of the rotary incinerator, the hull outside of the tertiary-air pipe and the revolution
The shell of formula incinerator is tangent.
2. burning processing system according to claim 1, which is characterized in that the burning processing system further include:
First machine oil spray gun, positioned at the interface of the tertiary-air pipe and the rotary incinerator, for the High Temperature Gas
Body heating；
Second machine oil spray gun, it is warm in the furnace for improving the rotary incinerator positioned at the top of the rotary incinerator
Degree；
Third machine oil spray gun, positioned at the top of the rotary incinerator, the straight section position of the dore furnace, towards the decomposition
In furnace, for maintaining the in-furnace temperature of the dore furnace.
3. burning processing system according to claim 2, which is characterized in that the first machine oil spray gun, second machine
The material that oily spray gun, the third machine oil spray gun spray is used oil.
4. burning processing system according to claim 1, which is characterized in that the dore furnace includes two sections, described
The upper section of dore furnace is straight section, and the lower section of the dore furnace is cone cell；And
The rotary incinerator is connected with the straight part of the dore furnace.
5. burning processing system according to claim 1, which is characterized in that the burning processing system is at least further include:
Feed lines are connected with the rotary incinerator, the addition for the waste；
First blanking air valve is located in the feed lines, for controlling the feeding capacity of the waste；
Second blanking air valve is located in the feed lines, for controlling the feeding capacity of the waste.
6. burning processing system according to claim 5, which is characterized in that the burning processing system further include:
Buffer unit is located in the feed lines, for reducing impact of the waste to the rotary incinerator；With
And
The buffer unit includes being selected from least one of beam type, chain type, grid type.
7. burning processing system according to claim 1, which is characterized in that the rotary incinerator includes:
Incinerator turntable, positioned at the bottom of the rotary incinerator, the rotation of waste described in the incinerator driven by rotary disc；
Fixed baffle is located in the rotary incinerator, treated for being discharged waste combustion residue.
8. burning processing system according to claim 7, which is characterized in that the burning processing system further include:
Cement kiln, the cement kiln are located at the lower section of the rotary incinerator and the dore furnace, the cement kiln and institute
Dore furnace is stated to be connected；And
The waste combustion treated the residue is discharged by the rotary incinerator, by the dore furnace, is fallen into
In the cement kiln.
9. burning processing system according to claim 7, which is characterized in that the incinerator turntable rotary is burnt with described
The sealing burnt between furnace shell uses flap seal form.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822167532.0U CN209672350U (en) | 2018-12-21 | 2018-12-21 | A kind of burning processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822167532.0U CN209672350U (en) | 2018-12-21 | 2018-12-21 | A kind of burning processing system |
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| Publication Number | Publication Date |
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| CN209672350U true CN209672350U (en) | 2019-11-22 |
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ID=68563144
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| CN201822167532.0U Active CN209672350U (en) | 2018-12-21 | 2018-12-21 | A kind of burning processing system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109539278A (en) * | 2018-12-21 | 2019-03-29 | 北京金隅北水环保科技有限公司 | A kind of burning processing system and incineration treatment method |
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2018
- 2018-12-21 CN CN201822167532.0U patent/CN209672350U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109539278A (en) * | 2018-12-21 | 2019-03-29 | 北京金隅北水环保科技有限公司 | A kind of burning processing system and incineration treatment method |
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