CN209484619U - Purification ash, which burns, utilizes device - Google Patents
Purification ash, which burns, utilizes device Download PDFInfo
- Publication number
- CN209484619U CN209484619U CN201822033344.9U CN201822033344U CN209484619U CN 209484619 U CN209484619 U CN 209484619U CN 201822033344 U CN201822033344 U CN 201822033344U CN 209484619 U CN209484619 U CN 209484619U
- Authority
- CN
- China
- Prior art keywords
- ash
- purification
- carbon materials
- pipeline
- transported
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
Abstract
The utility model relates to field of industrial machinery, more particularly to purification ash to burn and utilize device.Part is provided comprising purification ash and carbon materials ash provides part, purification ash provides part and provides pipeline comprising purification ash, purification ash provides pipeline and is connected to surge tank one, surge tank is connected to bag filter, the pipeline of bag filter connection is connected to combustion chamber by purifying grey inlet tube, purification ash after bag filter dedusting can be transported to combustion chamber by pump, and it includes carbon materials ash cellar that the carbon materials ash, which provides part, and ash in carbon materials ash cellar can be transported in combustion chamber by pump.Ash will be purified by transport tank for bulk materials vehicle to be transported in the purification ash feed bin being arranged by semi-coke drying system from furnace of calcium carbide purification system dirt nitrogen ash cellar, transportation tank car is extremely purified grey feed bin and conveyed using nitrogen.The purification ash purified in grey feed bin is drawn off through orlop portion, and purification ash is transported to fluidized bed furnace by pneumatic ash transmitting system and carries out burning utilization.
Description
Technical field
The utility model relates to field of industrial machinery, more particularly to purification ash to burn and utilize device.
Background technique
In process of production, furnace gas generates a large amount of purification ash to closed calcium carbide furnace after dry method dust, all regards before
It falls landfill disposal outside solid waste, causes environmental pollution and wasting of resources phenomenon (purification ash contains 8-10% fixed carbon).It is existing
Engineering technology is will to purify ash and burn by pneumatic conveying to raw material of wood-charcoal drying fluidized bed furnace to utilize, but this technology and construction investment
Higher, general enterprise is difficult to bear.
Utility model content
The purpose of utility model: it purifies ash preferably in order to provide a kind of effect and burns using device, specific purposes are shown in tool
Multiple substantial technological effects of body implementation section.
In order to reach purpose as above, the utility model adopts the following technical scheme:
Purification ash, which burns, utilizes device, which is characterized in that provides part comprising purification ash and carbon materials ash provides part, purification
Ash provides part and provides pipeline comprising purifying ash, purifies ash offer pipeline and is connected to surge tank one, surge tank is connected to cloth bag and removes
Dirt device, the pipeline of bag filter connection are connected to combustion chamber by purifying grey inlet tube, and pump can be by bag filter dedusting
Purification ash afterwards is transported to combustion chamber, and it includes carbon materials ash cellar that the carbon materials ash, which provides part, and pump can will be grey in carbon materials ash cellar
It is transported in combustion chamber.
The further technical solution of the utility model is that the avris of the pump of conveying purification ash is connected to air blower by pipeline
One.
The further technical solution of the utility model is that the avris for conveying the pump of carbon materials ash is connected to air blower by pipeline
Two.
The further technical solution of the utility model is that the combustion chamber avris is dispersed with secondary furnace and flying dust room.
It using the utility model of technical solution as above, has the advantages that compared with the existing technology: passing through bulk
Material transportation tank car is transported to the purification ash material being arranged by semi-coke drying system from furnace of calcium carbide purification system dirt nitrogen ash cellar for ash is purified
In storehouse, transportation tank car to the grey feed bin of purification is conveyed using nitrogen.The purification ash purified in grey feed bin is drawn off through orlop portion, by strength
Purification ash is transported to fluidized bed furnace and carries out burning utilization by ash-transmission system.Purification ash clinker after burning is from fluidized bed furnace burner hearth bottom
Discharge inhales apparatus for ash by negative pressure, collects and concentrates outward transport in purifying grey clinker warehouse.Purification ash is saved compared with prior art
It purifies from furnace of calcium carbide to fluidized bed furnace to purify the transportation system of grey feed bin and purify grey clinker and slag tap cold dryer system.
Detailed description of the invention
In order to further illustrate the utility model, it is further illustrated with reference to the accompanying drawing:
Fig. 1 is utility model structural schematic diagram；Wherein: 1. surge tanks one；2. bag filter；3. air blower one；4. drum
Blower two；5. pump；6. carbon materials ash cellar；7. purifying grey inlet tube；8. combustion chamber；9. secondary furnace；10. flying dust room；11. carbon materials ash into
Mouthful.
Specific embodiment
With reference to the accompanying drawings and detailed description, the utility model is furtherd elucidate, it should be understood that following specific embodiment parties
Formula is merely to illustrate the utility model rather than limitation the scope of the utility model.It needs in the description of the present invention,
Illustrate, term " center ", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outside", "top", "bottom" etc. refer to
The orientation or positional relationship shown be based on the orientation or positional relationship shown in the drawings, be merely for convenience of description the utility model and
Simplify description, rather than the device or element of indication or suggestion meaning must have a particular orientation, with specific orientation construction
And operation, therefore should not be understood as limiting the present invention.Furthermore unless specifically defined or limited otherwise, term " peace
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, be also possible to be electrically connected；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
The concrete meaning of language in the present invention.
This patent provides a variety of concomitant regimens, in place of different expression, belong to modified scheme based on basic scheme or
It is parallel type scheme.Every kind of scheme has the unique features of oneself.
Purification ash, which burns, utilizes device, which is characterized in that provides part comprising purification ash and carbon materials ash provides part, purification
Ash provides part and provides pipeline comprising purifying ash, purifies ash offer pipeline and is connected to surge tank 1, surge tank is connected to cloth bag and removes
Dirt device 2, the pipeline of bag filter connection are connected to combustion chamber by purifying grey inlet tube, and pump can be by bag filter dedusting
Purification ash afterwards is transported to combustion chamber, and it includes carbon materials ash cellar 6 that the carbon materials ash, which provides part, and pump can will be in carbon materials ash cellar 6
Ash is transported in combustion chamber.The technical effect and its realization process for the essence that the technical solution at this place is played are as follows: buffering
Tank can will purify ash by transport tank for bulk materials vehicle and be transported to from furnace of calcium carbide purification system dirt nitrogen ash cellar as grey feed bin is purified
In the purification ash feed bin being arranged by semi-coke drying system, transportation tank car to the grey feed bin of purification is conveyed using nitrogen.Purify grey feed bin
Interior purification ash is drawn off through orlop portion, and purification ash is transported to fluidized bed furnace by pneumatic ash transmitting system and carries out burning utilization.Through burning
Purification ash clinker afterwards is discharged from fluidized bed furnace burner hearth bottom, inhales apparatus for ash by negative pressure, collects and collects in purifying grey clinker warehouse
Middle outward transport.Purification ash is saved compared with prior art purify from furnace of calcium carbide to fluidized bed furnace purify the transportation system of grey feed bin and net
Ashing clinker is slagged tap cold dryer system.
The avris of the pump of conveying purification ash is connected to air blower one by pipeline.The avris for conveying the pump of carbon materials ash passes through pipe
Road is connected to air blower two.The combustion chamber avris is dispersed with secondary furnace and flying dust room.
In a creative way, above each effect is individually present, moreover it is possible to the combination of the above results is completed with a nested structure.
It is clear that the technical effect that the above structure is realized is realized, if the additional technical solution is not taken into account, this patent title is also
It can be a kind of new type purification ash combustion system.
It should be noted that multiple schemes that this patent provides include the basic scheme of itself, independently of each other, not mutually
It restricts, but it can also be combined with each other in the absence of conflict, reach multiple effects and realize jointly.
As nonessential expansion: purification dust heap density is about 0.3 ton/cube, and partial size is superfine, and about 40-120 DEG C of temperature,
Water content is low, flows freely.About 60 tons are produced daily, converts into 200m3, burnt down by 20 hours, then burns about 3.0 tons per hour, are converted into
10m3, two fluidized bed furnace consumption, i.e. every fluidized bed furnace need 1.5 tons of (5m3)/hours of conveying capacity.Purify grey feed bin height about 10
Purification ash is transported to drying kiln by pipeline gas conveying, is burnt by burner by rice.As a further preference,
This programme installs 2 powder level-one atomizers in the case where purifying grey feed bin tapering frequency conversion Star-like unloader, and purification ash passes through frequency conversion star
Type discharger enters in atomizer cavity, and the material for fluidizing state is sent into boiling by 102 × 6mm seamless steel pipe by primary air fan
Rise furnace burning.
Basic principles, main features, and advantages of the present invention has been shown and described above.Ability
The technical staff in domain should be recognized that the present utility model is not limited to the above embodiments, described in the above embodiment and specification
Only illustrate the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model can also
There are various changes and modifications, these changes and improvements are both fallen in claimed range.
Claims (4)
1. purification ash, which burns, utilizes device, which is characterized in that provide part comprising purification ash and carbon materials ash provides part, purification ash
Part is provided and provides pipeline comprising purifying ash, ash offer pipeline is provided and is connected to surge tank one (1), surge tank one is connected to cloth bag
Deduster (2), the pipeline of bag filter connection are connected to combustion chamber by purifying grey inlet tube, and pump can be by bag filter
Purification ash after dedusting is transported to combustion chamber, and it includes carbon materials ash cellar (6) that the carbon materials ash, which provides part, and pump can be by carbon materials ash
Ash is transported in combustion chamber in storehouse (6).
2. purification ash as described in claim 1, which burns, utilizes device, which is characterized in that the avris of the pump of conveying purification ash passes through
Pipeline is connected to air blower one.
3. purification ash as described in claim 1, which burns, utilizes device, which is characterized in that the avris of the pump of conveying carbon materials ash passes through
Pipeline is connected to air blower two.
4. purification ash as described in claim 1, which burns, utilizes device, which is characterized in that the combustion chamber avris is dispersed with combustion
Room and flying dust room to the greatest extent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822033344.9U CN209484619U (en) | 2018-12-05 | 2018-12-05 | Purification ash, which burns, utilizes device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822033344.9U CN209484619U (en) | 2018-12-05 | 2018-12-05 | Purification ash, which burns, utilizes device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209484619U true CN209484619U (en) | 2019-10-11 |
Family
ID=68118009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822033344.9U Active CN209484619U (en) | 2018-12-05 | 2018-12-05 | Purification ash, which burns, utilizes device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209484619U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112128772A (en) * | 2020-09-08 | 2020-12-25 | 新疆中泰矿冶有限公司 | Comprehensive solid waste recycling device and using method thereof |
-
2018
- 2018-12-05 CN CN201822033344.9U patent/CN209484619U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112128772A (en) * | 2020-09-08 | 2020-12-25 | 新疆中泰矿冶有限公司 | Comprehensive solid waste recycling device and using method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103759546A (en) | Calcium carbide furnace purification ash back-to-furnace combustion system | |
| JP2013512176A (en) | Powder lime baking method and apparatus | |
| CN101776269B (en) | N-level incineration treatment technology for domestic garbage | |
| CN103435276B (en) | Production apparatus of active lime | |
| CN203672164U (en) | Purified ash returning combustion system of calcium carbide furnace | |
| CN110469857B (en) | Waste incineration and hazardous waste plasma gasification parallel coupling treatment system and process | |
| CN103626409B (en) | Method and device for treatment in feeding household garbage into cement kiln in three routes | |
| CN108036323A (en) | The system and method that cement kiln cooperates with multifuel combustion garbage flying ash and sludge eco-cement | |
| CN101265041B (en) | Technique for using dry discharging carbide slag to completely substitute natural calcareous raw material for producing cement chamotte | |
| CN102863061A (en) | Drying energy-saving method and device for producing polyaluminium chloride water purifying agent | |
| CN209484619U (en) | Purification ash, which burns, utilizes device | |
| CN110639318B (en) | Environment-friendly and energy-saving coal calcining system and method thereof | |
| CN108502884A (en) | A method of producing the grey mix and convert calcium lime powder pressure ball molding of calcium carbide furnace of calcium carbide purification | |
| CN111006220A (en) | Industry is useless admittedly and is burnt system in coordination with mud | |
| CN114517915A (en) | System and process method for preparing ceramsite by combining waste incineration and sludge | |
| CN112762461A (en) | Sludge incineration equipment | |
| CN105157022A (en) | Horizontal circulating fluidized bed boiler with bed material out circulation function | |
| CN211813457U (en) | System for catching and purifying carbon dioxide in cement clinker production line | |
| CN104548920A (en) | Desulfurization device and desulfurization method | |
| CN111365718A (en) | Novel fluidized bed adiabatic incinerator for dried sludge and treatment method | |
| CN205774328U (en) | Fine coal fast pyrolysis systems | |
| CN101492256A (en) | Method for directly burning calcium carbide furnace gas to manufacture lime by using rotary kiln | |
| CN204073839U (en) | Devulcanizing pan | |
| CN103160300A (en) | Modification quality upgrading system of brown coal | |
| CN201660563U (en) | Shaft furnace of powdered coal gasification limekiln |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |