CN201301287Y - Magnesium metal smelting slag treatment and recycling system - Google Patents
Magnesium metal smelting slag treatment and recycling system Download PDFInfo
- Publication number
- CN201301287Y CN201301287Y CNU2008201061801U CN200820106180U CN201301287Y CN 201301287 Y CN201301287 Y CN 201301287Y CN U2008201061801 U CNU2008201061801 U CN U2008201061801U CN 200820106180 U CN200820106180 U CN 200820106180U CN 201301287 Y CN201301287 Y CN 201301287Y
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- CN
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- magnesium metal
- pipeline
- metal smelting
- dust collector
- type dust
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- Expired - Fee Related
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Abstract
The utility model relates to a magnesium metal smelting slag treatment and recycling system, belonging to magnesium metal smelting high-temperature slag treatment and recycling technical field. Aiming to provide a magnesium metal smelting slag treatment and recycling system which can thoroughly absorb the afterheat and soot of the slag, and reduce the soot pollution, the utility model adopts the technical proposal that a cooler is connected below a cooling bunker; a bucket elevator is connected below the cooler through a pipeline; the outlet of the buckle elevator is arranged above the hopper of a storage hopper; a soot discharge device is connected below the storage hopper; air suction hoods are arranged above the cooling hopper and the storage hopper and are connected with a pulse bag type dust collector; the grain discharge port of the pulse bag type dust collector extends into the cooling hopper through a pipeline; and the fume discharge port of the pulse bag type dust collector is connected with a blower set and then is connected to a chimney through a pipeline. The magnesium metal smelting slag treatment and recycling system is widely applicable in magnesium metal slag treatment field.
Description
Technical field
The utility model magnesium metal smelting controlling waste residue and cyclic utilization system belong to high temperature controlling waste residue and recycle utilization field behind the magnesium metal smelting.
Background technology
Generally about 800 ℃, the high temperature waste residue carries transportation inconvenient to the waste residue temperature that produces in the magnesium metal smelting process, brings potential safety hazard to workman's work; High temperature waste residue water for cooling, temperature-fall period produces a large amount of flue gases, and the waste residue after the cooling can not be used because of meeting the water caking again, this processing mode waste resource, contaminate environment.
The utility model content
For solving the problem that prior art exists, problem to be solved in the utility model is: a kind of improvement magnesium metal smelting waste residue and cyclic utilization system are provided, fully absorb waste residue waste heat and flue dust, reduce smoke contamination.
In order to address the above problem, the scheme that the utility model adopts is: magnesium metal smelting controlling waste residue and cyclic utilization system, the below of cooling feed bin is connected the left side of water cooler, the below, right side of water cooler is connected the below of bucket elevator by pipeline, the top outlet of bucket elevator is positioned at the hopper top of Storage Silo, the below of Storage Silo connects ash-discharging device, above cooling feed bin and Storage Silo, be provided with air-suction cover, air-suction cover is connected the ingress of pulse bag type dust collector by pipeline, the solid particulate relief outlet of pulse bag type dust collector stretches in the cooling feed bin by pipeline, and the flue gas discharge opening of pulse bag type dust collector inserts chimney after connecting the ventilation unit by pipeline.
The advantage of the utility model magnesium metal smelting controlling waste residue and cyclic utilization system is that flow process is reasonable, and is reliable for effect, and dry waste residue utilizes as industrial raw material again; Dusty gas is purified, and economizes on resources the protection environment.
Description of drawings
Below in conjunction with accompanying drawing the utility model is described further:
Fig. 1 is the synoptic diagram of the utility model magnesium metal smelting controlling waste residue and cyclic utilization system.
Wherein: 1-flour dust transport vehicle, 2-ash-discharging device, 3-Storage Silo, 4-bucket elevator, 5-water cooler, 6-cooling feed bin, 7-pulse bag type dust collector, 8-dedusting ventilator, 9-chimney, 10-air-suction cover 10.
Embodiment
Magnesium metal smelting controlling waste residue and cyclic utilization system among Fig. 1, structure is: the below of cooling feed bin 6 is connected the left side of water cooler 5, the below, right side of water cooler 5 is connected the below of bucket elevator 4 by pipeline, the top outlet of bucket elevator 4 is positioned at the hopper top of Storage Silo 3, the below of Storage Silo 3 connects ash-discharging device 2, the below of ash-discharging device 2 is provided with flour dust transport vehicle 1, above cooling feed bin 6 and Storage Silo 3, be provided with air-suction cover 10, air-suction cover 10 pass through the ingress that pipeline is connected pulse bag type dust collector 7, the solid particulate relief outlet of pulse bag type dust collector 7 stretches in the cooling feed bin 6 by pipeline, and the flue gas discharge opening of pulse bag type dust collector 7 connects ventilation unit 8 backs by pipeline and inserts chimney 9.
This working process is: magnesium metal smelting high temperature waste residue by artificial conveyance to the cooling feed bin 6, after cooling feed bin 6 is kept in, be transported to water cooler 5, water cooler 5 can adopt the surface heat exchanging mode, cooled waste residue is dry waste residue, the waste residue waste heat has obtained abundant recovery, and dry waste residue utilizes as industrial raw material again; Flow into bucket elevator 4 through water cooler 5 cooled waste residues, be transported to Storage Silo 3 by bucket elevator 4 and store, sent by waggon 1 at last, dry waste residue utilizes as industrial raw material again.In the waste residue process of cooling when overcooling feed bin 6 and Storage Silo 3, the dusty gas of its generation is collected through air-suction cover 10, entering pulse bag type dust collector 7 purifies, effect lower stack 9 at ventilation unit 8 enters atmosphere, recycles after entering secondary combustion or passing through the cleaning apparatus dedusting of chimney 9 again.
Claims (1)
1, magnesium metal smelting controlling waste residue and cyclic utilization system, it is characterized in that: the below of cooling feed bin (6) is connected the left side of water cooler (5), the below, right side of water cooler (5) is connected the below of bucket elevator (4) by pipeline, the top outlet of bucket elevator (4) is positioned at the hopper top of Storage Silo (3), the below of Storage Silo (3) connects ash-discharging device (2), top in cooling feed bin (6) and Storage Silo (3) is provided with air-suction cover (10), air-suction cover (10) is connected the ingress of pulse bag type dust collector (7) by pipeline, the solid particulate relief outlet of pulse bag type dust collector (7) stretches in the cooling feed bin (6) by pipeline, and the flue gas discharge opening of pulse bag type dust collector (7) connects ventilation unit (8) back by pipeline and inserts chimney (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201061801U CN201301287Y (en) | 2008-10-10 | 2008-10-10 | Magnesium metal smelting slag treatment and recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201061801U CN201301287Y (en) | 2008-10-10 | 2008-10-10 | Magnesium metal smelting slag treatment and recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201301287Y true CN201301287Y (en) | 2009-09-02 |
Family
ID=41084909
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201061801U Expired - Fee Related CN201301287Y (en) | 2008-10-10 | 2008-10-10 | Magnesium metal smelting slag treatment and recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201301287Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103086168A (en) * | 2013-01-25 | 2013-05-08 | 福建永恒能源管理有限公司 | Coal ash catch, storage and delivery system |
| CN114345700A (en) * | 2021-12-17 | 2022-04-15 | 府谷县泰达煤化有限责任公司 | Sorting device for magnesium reducing slag and comprehensive treatment device and treatment method thereof |
-
2008
- 2008-10-10 CN CNU2008201061801U patent/CN201301287Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103086168A (en) * | 2013-01-25 | 2013-05-08 | 福建永恒能源管理有限公司 | Coal ash catch, storage and delivery system |
| CN114345700A (en) * | 2021-12-17 | 2022-04-15 | 府谷县泰达煤化有限责任公司 | Sorting device for magnesium reducing slag and comprehensive treatment device and treatment method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090902 Termination date: 20131010 |