CN208810794U - A kind of lime-ash plasma melting proportioner and lime-ash plasma melting system - Google Patents
A kind of lime-ash plasma melting proportioner and lime-ash plasma melting system Download PDFInfo
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- CN208810794U CN208810794U CN201820798925.9U CN201820798925U CN208810794U CN 208810794 U CN208810794 U CN 208810794U CN 201820798925 U CN201820798925 U CN 201820798925U CN 208810794 U CN208810794 U CN 208810794U
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- storehouse
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- flying dust
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Abstract
It includes: flying dust storehouse that the utility model, which provides a kind of lime-ash plasma melting proportioner and lime-ash plasma melting system, the lime-ash plasma melting proportioner, burns the flying dust generated by incinerator to accommodate；The bottom ash generated is burned by the incinerator to accommodate in bottom ash storehouse；And blending bunker, the blending bunker are connected to the flying dust storehouse and the bottom ash storehouse, the flying dust conveyed by the flying dust storehouse to be mixed with the bottom ash conveyed by the bottom ash storehouse, wherein be provided with drying device in the blending bunker.Lime-ash plasma melting proportioner and lime-ash plasma melting system according to the present utility model, drying device is set in blending bunker, realize mixing and dry integrated setting, on the one hand reduce equipment investment occupied area, on the other hand transmission process of the material when being delivered to independent drying machine after mixing is avoided, so as to avoid the secondary pollution that may cause in material transportation process.
Description
Technical field
The utility model relates to incineration treatment of garbage fields, in particular to a kind of lime-ash plasma melting proportioner
With lime-ash plasma melting system.
Background technique
With the continuous expansion of city numbers and scale, the requirement to treatment of urban garbage is higher and higher.Waste incineration is made
For economic, efficient refuse disposal scheme, has the characteristics that innoxious, minimizing, recycling, obtained extensively in China in recent years
General development.
The flying dust and danger wastes that consumer waste incineration generates burn the flying dust generated and bottom ash belongs to dangerous give up
Gurry scope, and the processing mode for being directed to such danger wastes at present is mainly security landfill, higher cost.Now pass through
Ion fusion technology can innoxious, volume reduction, recycling by flying dust and bottom ash.It is pre- to locate in entire plasma melting system
Reason system is that entire project can run successful key, and ingredient drying device is the core equipment of pretreatment system.At present
Most common mode is that flying dust, bottom ash and additive enter belt after three storehouse mixings or the drying machine of other forms is done
It is dry.Ingredient and drying system separation, are attached by belt or other conveying equipments.It is followed by drying machine in three storehouse blenders,
Traditional drying equipment investment land occupation is bigger, while three storehouse blenders will appear material leakage in material transportation process, cause secondary
Pollution.
For this reason, it is necessary to propose a kind of new lime-ash plasma melting proportioner and lime-ash plasma melting system, use
To solve the problems of the prior art.
Utility model content
A series of concept of reduced forms is introduced in utility model content part, this will be in specific embodiment part
Middle further description.The utility model content part of the utility model is not meant to attempt to limit claimed
Technical solution key feature and essential features, do not mean that the guarantor for attempting to determine technical solution claimed more
Protect range.
The utility model provides a kind of lime-ash plasma melting proportioner, comprising:
The flying dust generated is burned by incinerator to accommodate in flying dust storehouse；
The bottom ash generated is burned by the incinerator to accommodate in bottom ash storehouse；And
Blending bunker, the blending bunker are connected to the flying dust storehouse and the bottom ash storehouse, will be conveyed by the flying dust storehouse
The flying dust mixed with the bottom ash conveyed by the bottom ash storehouse, wherein be provided with drying in the blending bunker
Device.
Illustratively, the flying dust storehouse and the bottom ash storehouse are disposed in parallel in the top of the blending bunker.
Illustratively, the flying dust storehouse is provided with gas dish arch breaking apparatus.
Illustratively, spiral conveying mechanism is provided between the flying dust storehouse and the blending bunker.
Illustratively, vibrating feeding mechanism is provided between the bottom ash storehouse and the blending bunker.
Illustratively, the drying device includes the hot coil being arranged in the outer wall interlayer of the blending bunker.
Illustratively, the flying dust storehouse and the bottom ash storehouse pass through respectively be flexible coupling with metal chute and the blending bunker into
Row connection.
Illustratively, the volume range of the blending bunker is 1-5 cubic metres.
Illustratively, the flying dust storehouse and/or the bottom ash storehouse are provided with weighing sensor, level sensor and wall surface vibration
Dynamic device.
The utility model additionally provides a kind of lime-ash plasma melting system, fills including ingredient described in any of the above one
It sets.
Lime-ash plasma melting proportioner and lime-ash plasma melting system according to the present utility model, in blending bunker
Drying device is set, realizes mixing and dry integrated setting, on the one hand reduces equipment investment occupied area, on the other hand
Transmission process of the material when being delivered to independent drying machine after mixing is avoided, so as to avoid possible in material transportation process
Caused by secondary pollution.
Detailed description of the invention
The following drawings of the utility model is used to understand the utility model in this as a part of the utility model.Attached drawing
In show the embodiments of the present invention and its description, for explaining the principles of the present invention.
In attached drawing:
Fig. 1 is the structural representation according to a kind of lime-ash plasma melting proportioner of one embodiment of the utility model
Figure.
Specific embodiment
In the following description, a large amount of concrete details are given more thoroughly to manage in order to provide to the utility model
Solution.It is, however, obvious to a person skilled in the art that the utility model may not need it is one or more of these thin
It saves and is carried out.In other examples, in order to avoid obscuring with the utility model, for more well known in the art
Technical characteristic is not described.
In order to thoroughly understand the utility model, detailed description will be proposed in following description, to illustrate that this is practical new
Proportioner described in type.Obviously, the execution of the utility model be not limited to incineration treatment of garbage field technical staff institute it is ripe
The specific details of habit.The preferred embodiment of the utility model is described in detail as follows, however other than these detailed descriptions, this is practical
It is novel to have other embodiments.
It should give it is noted that term used herein above is merely to describe specific embodiment, and be not intended to restricted root
According to the exemplary embodiment of the utility model.As used herein, unless the context clearly indicates otherwise, otherwise singular shape
Formula is also intended to include plural form.Additionally, it should be understood that when using term "comprising" and/or " packet in the present specification
Include " when, indicate that there are the feature, entirety, step, operation, element and/or component, but do not preclude the presence or addition of one
Or other multiple features, entirety, step, operation, element, component and/or their combination.
Now, exemplary embodiment according to the present utility model is more fully described with reference to the accompanying drawings.However, these examples
Property embodiment can be implemented with many different forms, and should not be construed to be limited solely to the embodiments set forth herein.
It should be understood that these embodiments are provided so that the utility model disclosure it is thoroughly and complete, and these are shown
The design of example property embodiment is fully conveyed to those of ordinary skill in the art.In the accompanying drawings, for the sake of clarity, exaggerate layer and
The thickness in region, and make that identical element is presented with like reference characters, thus description of them will be omitted.
The flying dust and danger wastes that consumer waste incineration generates burn the flying dust generated and bottom ash belongs to dangerous give up
Gurry scope, and the processing mode for being directed to such danger wastes at present is mainly security landfill, higher cost.Now pass through
Ion fusion technology can innoxious, volume reduction, recycling by flying dust and bottom ash.It is pre- to locate in entire plasma melting system
Reason system is that entire project can run successful key, and ingredient drying device is the core equipment of pretreatment system.At present
Most common mode is that flying dust, bottom ash and additive enter belt after three storehouse mixings or the drying machine of other forms is done
It is dry.Ingredient and drying system separation, are attached by belt or other conveying equipments.It is followed by drying machine in three storehouse blenders,
Traditional drying equipment investment land occupation is bigger, and three storehouse blenders will appear material leakage in material transportation process, cause secondary dirt
Dye.
Embodiment one
In order to solve the problems in the prior art, the utility model provides a kind of lime-ash plasma melting proportioner,
Include:
The flying dust generated is burned by incinerator to accommodate in flying dust storehouse；
The bottom ash generated is burned by the incinerator to accommodate in bottom ash storehouse；And
Blending bunker, the blending bunker are connected to the flying dust storehouse and the bottom ash storehouse, will be conveyed by the flying dust storehouse
The flying dust mixed with the bottom ash conveyed by the bottom ash storehouse, wherein be provided with drying in the blending bunker
Device.
It is schematically illustrated below with reference to lime-ash plasma melting proportioner of the Fig. 1 to the utility model, wherein Fig. 1
For according to a kind of structural schematic diagram of lime-ash plasma melting proportioner of one embodiment of the utility model.
Referring to Fig. 1, a kind of lime-ash plasma melting proportioner according to the present utility model includes flying dust storehouse 1, flying dust storehouse 1
The flying dust generated is burned by incinerator to accommodate；The bottom ash generated is burned by incinerator to accommodate in bottom ash storehouse 2, bottom ash storehouse 2；
And blending bunker 3, blending bunker 3 are connected to flying dust storehouse 1 and bottom ash storehouse 2, to the flying dust that will be conveyed by the flying dust storehouse 1 with by institute
The bottom ash for stating the conveying of bottom ash storehouse 2 is mixed, wherein drying device 4 is provided in the blending bunker.It is arranged in blending bunker
Drying device realizes mixing and dry integrated setting, on the one hand reduces equipment to be dried in mixing process
Occupied area is invested, transmission process of the material when being delivered to independent drying machine after mixing is on the other hand avoided, to keep away
The secondary pollution that may cause in material transportation process is exempted from.
Illustratively, referring to Fig. 1, the flying dust storehouse 1 is disposed in parallel in the upper of the blending bunker 3 with the bottom ash storehouse 2
Side.To, the flying dust that is inputted by flying dust storehouse 1 and blending bunker 3 is fallen directly by the bottom ash that bottom ash storehouse 2 inputs, on the one hand further
Increase the integrated level of proportioner, on the other hand simplifies transmission process.
Illustratively, with continued reference to Fig. 1, weighing sensor is provided on the flying dust storehouse 1 and the bottom ash storehouse 2
(not shown), wall surface vibrator 101 and 201, level sensor 102 and 202.Wherein, weighing sensor is used to flying dust storehouse
Bottom ash in flying dust and bottom ash storehouse carries out proportion when flying dust and bottom ash mixing are realized in weighing.Wall Vibration device is to make flying dust storehouse
It is shaken with the wall surface in bottom ash storehouse, reduces the attachment of flying dust and bottom ash on flying dust storehouse and bottom ash storehouse, prevent flying dust storehouse and bottom
The putty in slag storehouse.Level sensor detects the material position of flying dust and bottom ash in flying dust storehouse and bottom ash storehouse, to control feed
Speed.Illustratively, in the present embodiment, flying dust storage capacity is no more than 12 hours consumptions, prevents volume is excessive from occurring to block up
Material.
For three storehouse blenders, due to the moisture-absorption characteristics of flying dust, bottom ash particle diameter distribution are wider etc., often will appear winged
Ash cellar putty, bottom ash batcher failure, cause the non-uniform phenomenon of mixing, influence the melting efficiency of rear end, more seriously may
Cause the stoppage in transit of system.Illustratively, with continued reference to Fig. 1, gas dish arch breaking apparatus 103, the gas dish are provided on flying dust storehouse 1
Arch breaking apparatus 103 carries out air-flow " liquefaction " to the flying dust that can not be flowed freely in flying dust storehouse, is caused to flow, so that maximum can
It can prevent flying dust storehouse putty.Further, illustratively, as shown in Figure 1, being provided between the flying dust storehouse 1 and the blending bunker 3
Spiral conveying mechanism 104, to the fly ash carry that falls flying dust storehouse 1 to blending bunker 3.Further, illustratively, such as Fig. 1 institute
Show, is provided with vibrating feeding mechanism 203 between the bottom ash storehouse 2 and the blending bunker 3.To prevent bulk bottom ash from conveying
Failure.It is to be appreciated that gas dish arch breaking apparatus 103, spiral conveying mechanism 104 and vibrating feeding mechanism are arranged in the present embodiment
203 are only exemplary, and those skilled in the art are also an option that other can prevent flying dust storehouse putty, the feed event of bottom ash storehouse
The device of barrier is configured at the utility model.
Illustratively, as shown in Figure 1, being provided with maintenance valve 105 and 204 in the bottom in flying dust storehouse 1 and bottom ash storehouse 2.
Illustratively, as shown in Figure 1, the drying device 4 includes the hot coil being arranged in 3 outer wall interlayer of blending bunker
401.The enlarged diagram of the drying device shown on the left of blending bunker 3 as shown in figure 1 has interlayer in the design of 3 outer wall of blending bunker
301, it include the hot coil 401 being arranged in interlayer 301, the hot plate that external heat source passes through design in interlayer 301 in drying device 4
Pipe 401 exchanges heat during mixing with material, to play the role of dried material.Drying device is set as being arranged
Hot coil in blending bunker outer wall interlayer, can make in blending bunker mixing process, and material is completely in the ring of hot coil heating
Border significantly improves uniform drying and drying efficiency.
Illustratively, the flying dust storehouse and/or the bottom ash storehouse are mixed with metal chute with underlying by being flexible coupling
Feed bin is attached, to guarantee the airtightness of device materials inside conveying, the flying dust being further reduced in transmission process and bottom
Pollution of the slag to environment.
Illustratively, the volume range of the blending bunker is 1-5 cubic metres.1-5 is set by the volume range of blending bunker
Cubic meter avoids the occurrence of that volume is excessive and mixing so that material is adequately mixed in mixing process by auger
Insufficient phenomenon.
As shown in Figure 1, being additionally provided with jumbo bag 5 in the bottom of blending bunker 3, mixed material is transported, to carry out
Lime-ash plasma melting.
In the present embodiment, lime-ash plasma melting proportioner is arranged to flying dust storehouse and bottom ash storehouse, blending bunker, jumbo bag
The structure arranged from top to bottom significantly increases the integrated level of system, reduces the occupied area of device.In one example, such as
Shown in Fig. 1, flying dust storehouse 1, bottom ash storehouse 2, blending bunker 3 and jumbo bag 5 are arranged on bracket 6, material transportation mechanism (not shown)
Material lifting is delivered to dust arrester installation 7, dust arrester installation 7 by flying dust dispensing to the dust collect plant 106 being located on flying dust storehouse 1 and
By lime-ash dispensing to the dust collect plant 205 being located on bottom ash storehouse 2, then, flying dust and lime-ash respectively fall in flying dust storehouse 1 and bottom ash
In storehouse 2, and further it is delivered to blending bunker 3 and is mixed.
Drying device is arranged in lime-ash plasma melting proportioner according to the present utility model in blending bunker, realizes mixed
Material and dry integrated setting, on the one hand reduce equipment investment occupied area, on the other hand avoid material mixing it
It is delivered to transmission process when independent drying machine, afterwards so as to avoid the secondary pollution that may cause in material transportation process.
Embodiment two
The utility model additionally provide a kind of lime-ash plasma melting system, including the lime-ash as shown in embodiment one etc. from
Sub- molten formulation device.Since the lime-ash plasma melting proportioner according to embodiment one realizes mixing and dry one
Change setting, reduces equipment investment occupied area, avoid conveying of the material when being delivered to independent drying machine after mixing
Journey, so as to avoid secondary pollution, lime-ash plasma melting system according to the present utility model also has above-mentioned advantage.
The utility model is illustrated through the foregoing embodiment, but it is to be understood that, above-described embodiment is
Purpose for illustrating and illustrating, and be not intended to limit the invention within the scope of described embodiment.Furthermore ability
Field technique personnel are it is understood that the utility model is not limited to above-described embodiment, and introduction according to the present utility model is also
More kinds of variants and modifications can be made, these variants and modifications all fall within the utility model range claimed with
It is interior.The protection scope of the utility model is defined by the appended claims and their equivalents.
Claims (10)
1. a kind of lime-ash plasma melting proportioner characterized by comprising
The flying dust generated is burned by incinerator to accommodate in flying dust storehouse；
The bottom ash generated is burned by the incinerator to accommodate in bottom ash storehouse；And
Blending bunker, the blending bunker are connected to the flying dust storehouse and the bottom ash storehouse, to the institute that will be conveyed by the flying dust storehouse
It states flying dust and is mixed with the bottom ash conveyed by the bottom ash storehouse, wherein be provided with drying device in the blending bunker.
2. lime-ash plasma melting proportioner as described in claim 1, which is characterized in that the flying dust storehouse and the bottom ash
Storehouse is disposed in parallel in the top of the blending bunker.
3. lime-ash plasma melting proportioner as described in claim 1, which is characterized in that the flying dust storehouse is provided with gas dish
Arch breaking apparatus.
4. lime-ash plasma melting proportioner as claimed in claim 2, which is characterized in that the flying dust storehouse and the mixing
Spiral conveying mechanism is provided between storehouse.
5. lime-ash plasma melting proportioner as claimed in claim 2, which is characterized in that the bottom ash storehouse and the mixing
Vibrating feeding mechanism is provided between storehouse.
6. lime-ash plasma melting proportioner as described in claim 1, which is characterized in that the drying device includes setting
Hot coil in the outer wall interlayer of the blending bunker.
7. lime-ash plasma melting proportioner as claimed in claim 2, which is characterized in that the flying dust storehouse and the bottom ash
Storehouse passes through to be flexible coupling respectively to be attached with metal chute and the blending bunker.
8. lime-ash plasma melting proportioner as described in claim 1, which is characterized in that the volume range of the blending bunker
It is 1-5 cubic metres.
9. lime-ash plasma melting proportioner as described in claim 1, which is characterized in that the flying dust storehouse and/or described
Bottom ash storehouse is provided with weighing sensor, level sensor and Wall Vibration device.
10. a kind of lime-ash plasma melting system, which is characterized in that including lime-ash as described in any one of claims 1-9
Plasma melting proportioner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820798925.9U CN208810794U (en) | 2018-05-24 | 2018-05-24 | A kind of lime-ash plasma melting proportioner and lime-ash plasma melting system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820798925.9U CN208810794U (en) | 2018-05-24 | 2018-05-24 | A kind of lime-ash plasma melting proportioner and lime-ash plasma melting system |
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| Publication Number | Publication Date |
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| CN208810794U true CN208810794U (en) | 2019-05-03 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111121058A (en) * | 2019-12-24 | 2020-05-08 | 上海和惠生态环境科技有限公司 | Fly ash treatment equipment |
-
2018
- 2018-05-24 CN CN201820798925.9U patent/CN208810794U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111121058A (en) * | 2019-12-24 | 2020-05-08 | 上海和惠生态环境科技有限公司 | Fly ash treatment equipment |
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