CN209685884U - A kind of clinker RO phase separation system - Google Patents
A kind of clinker RO phase separation system Download PDFInfo
- Publication number
- CN209685884U CN209685884U CN201822228165.0U CN201822228165U CN209685884U CN 209685884 U CN209685884 U CN 209685884U CN 201822228165 U CN201822228165 U CN 201822228165U CN 209685884 U CN209685884 U CN 209685884U
- Authority
- CN
- China
- Prior art keywords
- clinker
- outlet
- storage tank
- concentration equipment
- filter
- 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.)
- Expired - Fee Related
Links
- 238000005191 phase separation Methods 0.000 title claims abstract description 12
- 238000000227 grinding Methods 0.000 claims abstract description 18
- 238000003825 pressing Methods 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims abstract description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 12
- 239000003546 flue gas Substances 0.000 claims description 12
- 238000004073 vulcanization Methods 0.000 claims description 11
- 210000004080 milk Anatomy 0.000 claims description 8
- 235000013336 milk Nutrition 0.000 claims description 8
- 239000006148 magnetic separator Substances 0.000 claims description 7
- 239000008267 milk Substances 0.000 claims description 7
- 238000007885 magnetic separation Methods 0.000 claims description 6
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 4
- 230000008676 import Effects 0.000 claims description 3
- 238000004062 sedimentation Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 235000019504 cigarettes Nutrition 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 239000003517 fume Substances 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 3
- 239000002893 slag Substances 0.000 description 6
- 239000002699 waste material Substances 0.000 description 6
- 229910052500 inorganic mineral Inorganic materials 0.000 description 5
- 239000011707 mineral Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 241000237858 Gastropoda Species 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 235000021321 essential mineral Nutrition 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000001238 wet grinding Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model relates to a kind of clinker RO phase separation system of environment protection field, discharging device is equipped with below storage device；Concentration equipment is equipped with below discharging device, concentration equipment is equipped with first outlet and second outlet separately below, first outlet is correspondingly arranged on the first agitating device, second outlet is equipped with the second agitating device, the first grinding device is equipped with below first agitating device, concentration equipment is provided below in first grinding device, front side outlet and rear side exit is provided below in concentration equipment, is respectively arranged with filter-pressing device below front side outlet and rear side exit；Collection device is provided below in filter-pressing device；Second agitating device is correspondingly arranged on output device；The utility model can quickly sort the RO phase in clinker, and carry out fume treatment to clinker before sorting, improve the stability of the separation system, while being also beneficial to be recycled clinker.
Description
Technical field
The utility model relates to clinker RO phase separation systems a kind of in environment protection field.
Background technique
A large amount of solid waste is generated in smelting iron and steel process, solid waste mainly includes slag (blast furnace granulated slag or water
Slag) and clinker (steelmaking wastes, waste residue)；It is ripe day by day for the processing technique of slag, and the processing of steel slag is still capable
A great problem in industry；The essential mineral group of clinker slag becomes three classes: silicates mineral (A mineral, B mineral)；TeO,MgO,
The oxide of CaO and FeO(Te, Mg, Mn are total to solution, i.e. RO phase) and Mg aluminate mineral；Traditional device mainly handles crystal
Material based on mineral, noise is big, and energy consumption is high；And processing is incomplete.
Utility model content
The purpose of the utility model is to provide a kind of clinker RO phase separation system, which can be to the RO in clinker
It is mutually quickly sorted, and fume treatment is carried out to clinker before sorting, improve the stability of the separation system, while
Be conducive to be recycled clinker.
Purpose of the utility model is realized as follows: a kind of clinker RO phase separation system, including feeding device, cooperate into
Expect the flue gas processing device of device setting；It is characterized in that, storage device is equipped with beside the feeding device, it is described
Discharging device is equipped with below storage device；Main concentration equipment, the magnetic separation are equipped with below the discharging device
Device is equipped with first outlet and second outlet separately below, and the first outlet is correspondingly arranged on the first agitating device,
The second outlet is equipped with the second agitating device, and the first grinding dress is equipped with below first agitating device
It sets, concentration equipment is provided below in first grinding device, front side outlet is provided below in the concentration equipment and rear side goes out
Mouthful, filter-pressing device is respectively arranged with below the front side outlet and rear side exit；Collection is provided below in the filter-pressing device
Device；Second agitating device is correspondingly arranged on output device.
When utility model works, starting output device, filter-pressing device, main concentration equipment, the first grinding device, first are stirred
Mix device, the second agitating device, concentration equipment, feeding device and its conveying device of cooperation apparatus above setting；Clinker passes through
Feeding device, which enters, carries out storage placement in storage device, the flue gas with sulfide generated with this clinker passes through at flue gas
It manages device and carries out suction process；The clinker being placed in storage device is transported to concentration equipment to containing RO phase by discharging device
Clinker carry out a magnetic separation, isolate waste material and fine fodder；Waste material enters the second agitating device by second outlet, is stirring
While endlessly carried out；Fine fodder enters in the first grinding device by the way that the first agitating device is continual
High speed shear is carried out, so that the broken mixing of fine fodder is complete；It is re-introduced into concentration equipment and carries out secondary magnetic separation, divided again
From the secondary slugs and secondary fine fodder isolated are squeezed by filter-pressing device.
The beneficial effects of the utility model are that the utility model can quickly sort the RO phase in clinker,
And fume treatment is carried out to clinker before sorting, the stability of the separation system is improved, while being also beneficial to carry out clinker
It recycles.
As a further improvement of the utility model, to guarantee a large amount of material of storage tank storage and convenient for later period holding foot
Enough supply amounts；The storage device includes several groups storage tank, is arranged below storage tank in cone setting, described several
Group storage tank is arranged side by side；The upper surface of each storage tank is equipped with feeding device, and the feeding device sequentially enters
In storage tank.
There is preferable treatment effect to flue gas for guarantee flue gas processing device as a further improvement of the utility model,；
The flue gas processing device includes the flue for being directly communicated to several groups storage tank, is arranged beside several groups storage tank for filtering
Filter, for the centrifugal blower of drawing smoke, the vulcanization tower for removing sulfide, setting vulcanization tower below precipitating
Pond；The middle part of filter and vulcanization tower is arranged in the centrifugal blower.
There is preferable grinding effect for the first agitating device of guarantee as a further improvement of the utility model,；It is described
First agitating device is in the bistrique storehouse of cone setting, the bistrique storehouse import of cooperation bistrique storehouse setting and the outlet of bistrique storehouse and its sets
Set the hopper in bistrique storehouse.
Fine grind can be carried out to material for the first grinding device of guarantee as a further improvement of the utility model,
Mill；First grinding device includes wet milk, and the concentration equipment includes wet magnetic separator, is arranged in wet milk and wet type magnetic
Select the vacuum pump between machine.
Detailed description of the invention
Fig. 1 is the main view of the utility model.
Fig. 2 is the partial front elevation view of the utility model.
Wherein, 1 feeding device, 2 flue gas processing devices, 3 discharging devices, 4 main concentration equipments, 5 first outlets, 6 second go out
Mouth, 7 first agitating devices, 8 second agitating devices, 9 first grinding devices, 10 concentration equipments, 11 front side outlets, 12 rear sides go out
Mouth, 13 filter-pressing devices, 14 output devices, 15 storage tanks, 16 flues, 17 filters, 18 centrifugal blowers, 19 vulcanization towers, 20 precipitatings
Pond, 21 bistrique storehouses, 22 wet milks, 23 wet magnetic separators, 24 vacuum pumps.
Specific embodiment
As shown in Figs. 1-2, purpose of the utility model is realized as follows: a kind of clinker RO phase separation system, including into
Expect the flue gas processing device 2 that device 1, cooperation feeding device 1 are arranged；The side of the feeding device 1 is equipped with storing dress
It sets, discharging device 3 is equipped with below the storage device；The discharging device 3 is equipped with main concentration equipment below
4, the concentration equipment 10 is equipped with first outlet 5 and second outlet 6 separately below, and the first outlet 5 is correspondingly arranged
There is the first agitating device 7, the second outlet 6 is equipped with the second agitating device 8, and first agitating device 7 is matched below
Conjunction is provided with the first grinding device 9, and first grinding device 9 is provided below under concentration equipment 10, the concentration equipment 10
Face is provided with front side outlet 11 and rear side exit 12, is respectively arranged with filters pressing below the front side outlet 11 and rear side exit 12
Device 13；Collection device is provided below in the filter-pressing device 13；Second agitating device 8 is correspondingly arranged on output device
14；The storage device includes several groups storage tank 15, is arranged below storage tank 15 in cone setting, the several groups storage
Batch can 15 is arranged side by side；The upper surface of each storage tank 15 is equipped with feeding device 1, and the feeding device 1 sequentially enters
Into storage tank 15；The flue gas processing device 2 includes the flue 16 for being directly communicated to several groups storage tank 15, is arranged in several groups
Filter 17, the centrifugal blower 18 for drawing smoke, the vulcanization for removing sulfide beside storage tank 15 for filtering
Sedimentation basin 20 below tower 19, setting vulcanization tower 19；The middle part of filter 17 and vulcanization tower 19 is arranged in the centrifugal blower 18；
First agitating device 7 is in the bistrique storehouse 21 of cone setting, 21 import of bistrique storehouse of cooperation bistrique storehouse 21 setting and bistrique
The hopper that storehouse 21 exports and its is arranged in bistrique storehouse 21；First grinding device 9 includes wet milk 22, the concentration equipment
10 include wet magnetic separator 23, the vacuum pump 24 being arranged between wet milk 22 and wet magnetic separator 23.
When utility model works, starting output device 14, filter-pressing device 13, main concentration equipment 4, the first grinding device 9,
First agitating device 7, the second agitating device 8, concentration equipment 10, feeding device 1 and its conveying dress of cooperation apparatus above setting
It sets；Clinker is entered by feeding device 1 and carries out storage placement in the several groups storage tank 15 of storage device, is generated with this clinker
The flue gas with sulfide enter vulcanization tower 19 by the flue 16 that is drawn into of centrifugal blower 18 and handled；It puts
The clinker set in storage device is transported to carrying out once to the clinker containing RO phase for main concentration equipment 4 by discharging device 3
Waste material and fine fodder are isolated in magnetic separation；Waste material enters the second agitating device 8 by second outlet 6, while agitating by a steady stream
Constantly carry out；Fine fodder passes through the continual bistrique storehouse 21 entered in the first grinding device 9 of the first agitating device 7
High speed shear is carried out, so that the broken mixing of fine fodder is complete；The wet milk 22 for being re-introduced into concentration equipment 10 carries out wet-milling, and its
Wet magnetic separator 23 carries out secondary magnetic separation, is separated again, and the secondary slugs and secondary fine fodder isolated pass through filter-pressing device
13 squeeze to get up finally to carry out.
The utility model is not limited to above-described embodiment, on the basis of technical solution disclosed by the utility model, this
For the technical staff in field according to disclosed technology contents, not needing creative labor can be special to some of which technology
Sign makes some replacements and deformation, these replacements and deformation are within the protection scope of the present utility model.
Claims (5)
1. a kind of clinker RO phase separation system, the flue gas processing device including feeding device, cooperation feeding device setting；Its feature
It is, storage device is equipped with beside the feeding device, is equipped with discharging device below the storage device；
Be equipped with main concentration equipment below the discharging device, the concentration equipment be equipped with separately below first outlet and
Second outlet, the first outlet are correspondingly arranged on the first agitating device, and the second outlet is equipped with the second stirring dress
It sets, the first grinding device is equipped with below first agitating device, magnetic separation is provided below in first grinding device
Front side outlet and rear side exit is provided below in device, the concentration equipment, divides below the front side outlet and rear side exit
Filter-pressing device is not provided with it；Collection device is provided below in the filter-pressing device；Second agitating device is correspondingly arranged on defeated
Device out.
2. a kind of clinker RO phase separation system according to claim 1, it is characterised in that: the storage device includes several
Group storage tank is arranged below storage tank in cone setting, and the several groups storage tank is arranged side by side；Each storage tank it is upper
Face is equipped with feeding device, and the feeding device sequentially enters in storage tank.
3. a kind of clinker RO phase separation system according to claim 1, it is characterised in that: the flue gas processing device includes
It is directly communicated to the flue of several groups storage tank, the filter for being used to filter beside several groups storage tank is set, for aspirating cigarette
The centrifugal blower of gas, the vulcanization tower for removing sulfide, the sedimentation basin below setting vulcanization tower；The centrifugal blower setting exists
The middle part of filter and vulcanization tower.
4. a kind of clinker RO phase separation system according to claim 1, it is characterised in that: first agitating device is in circle
The material that the bistrique storehouse of taper setting, the bistrique storehouse import of cooperation bistrique storehouse setting and bistrique storehouse export and its be arranged in bistrique storehouse
Slot.
5. a kind of clinker RO phase separation system according to claim 1, it is characterised in that: first grinding device includes
Wet milk, the concentration equipment includes wet magnetic separator, the vacuum pump that is arranged between wet milk and wet magnetic separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822228165.0U CN209685884U (en) | 2018-12-28 | 2018-12-28 | A kind of clinker RO phase separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822228165.0U CN209685884U (en) | 2018-12-28 | 2018-12-28 | A kind of clinker RO phase separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209685884U true CN209685884U (en) | 2019-11-26 |
Family
ID=68597267
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822228165.0U Expired - Fee Related CN209685884U (en) | 2018-12-28 | 2018-12-28 | A kind of clinker RO phase separation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209685884U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109554552A (en) * | 2018-12-28 | 2019-04-02 | 扬州市顺达科技有限公司 | A kind of clinker RO phase separation system and working method |
-
2018
- 2018-12-28 CN CN201822228165.0U patent/CN209685884U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109554552A (en) * | 2018-12-28 | 2019-04-02 | 扬州市顺达科技有限公司 | A kind of clinker RO phase separation system and working method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20191126 |