CN203917157U - Broken ferrophosphorus iron charcoal separator - Google Patents
Broken ferrophosphorus iron charcoal separator Download PDFInfo
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- CN203917157U CN203917157U CN201420346714.3U CN201420346714U CN203917157U CN 203917157 U CN203917157 U CN 203917157U CN 201420346714 U CN201420346714 U CN 201420346714U CN 203917157 U CN203917157 U CN 203917157U
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- roller
- ferrophosphorus
- broken
- screen cloth
- conveyer belt
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Abstract
The utility model provides a kind of broken ferrophosphorus iron charcoal separator, described broken ferrophosphorus iron charcoal separator comprises power set, the first roller, the second roller, conveyer belt and be located at the screening plant under described the first roller, described power set drive described the first roller and the second roller to rotate and interlock described in conveyer belt, described the first roller is permanent magnetism roller, described screening plant comprises screen cloth and is connected to the baffle plate of described screen bottom, the aperture of described screen cloth is 3～5mm, the angle of described screen cloth and described horizontal plane is 40 °～60 °, described baffle plate is 1/5～2/5 of described screen cloth length to the distance of the side of close described second roller of described screen cloth.Compared with correlation technique, the utility model beneficial effect is, effectively separates the powdered carbon in broken ferrophosphorus, reduces powdered carbon content in broken ferrophosphorus, improves ferrophosphorus burn-off rate, reduces power consumption, enhances productivity.
Description
[technical field]
The utility model relates to anode technology field, relates in particular to a kind of broken ferrophosphorus iron charcoal separator.
[background technology]
In aluminium industry, anode comprises guide rod, steel pawl, ferrophosphorus ring and charcoal piece, and wherein, steel pawl is connected with charcoal piece by ferrophosphorus ring.Along with the carrying out producing, charcoal piece is constantly consumed, and the anode of charcoal piece consumption is called as anode scrap.Because ferrophosphorus ring is only for connecting steel receiving grab and charcoal piece, do not participate in other reaction in production process, so ferrophosphorus ring does not exist loss in process of production, and can reclaim and recycle by fragmentation.But when the broken recovery of ferrophosphorus ring, owing to remaining charcoal piece on anode scrap, be broken in the process of broken ferrophosphorus at ferrophosphorus ring, charcoal piece is also fractured into powdered carbon and is entrained in broken ferrophosphorus as impurity.The broken ferrophosphorus that contains powdered carbon enters after intermediate frequency furnace, slows down because the existence of impurity causes ferrophosphorus burn-off rate, and intermediate frequency furnace power consumption increases, if it is more to fall to the impurity of intermediate frequency furnace bottom, also needs blowing out to carry out impurity cleaning, causes production efficiency to reduce.Thereby, effectively separate the powdered carbon in broken ferrophosphorus, reduce powdered carbon content in broken ferrophosphorus, improve ferrophosphorus burn-off rate, reduce power consumption, enhance productivity and become those skilled in the art and need badly the technical problem of solution.
Therefore, be necessary in fact to provide a kind of new broken ferrophosphorus iron charcoal separator to overcome above-mentioned technical problem.
[utility model content]
Technical problem to be solved in the utility model is to provide a kind of powdered carbon content in broken ferrophosphorus that effectively reduces, and improves ferrophosphorus burn-off rate, reduces power consumption, the broken ferrophosphorus iron charcoal separator of enhancing productivity.
A kind of broken ferrophosphorus iron charcoal separator of the utility model, described broken ferrophosphorus iron charcoal separator comprises power set, the first roller, be positioned at described the first roller right side and with described the first roller the second roller separated by a distance, be sheathed on the conveyer belt outside described the first roller and described the second roller simultaneously and be located at the screening plant under described the first roller, described power set drive described the first roller and the second roller to rotate and interlock described in conveyer belt, described the first roller is permanent magnetism roller, described screening plant comprises screen cloth and is connected to the baffle plate of described screen bottom, one end away from described the second roller of described screen cloth is positioned at the top near one end of described the second roller, the aperture of described screen cloth is 3～5mm, the angle of described screen cloth and described horizontal plane is 40 °～60 °, described baffle plate is 1/5～2/5 of described screen cloth length to the distance of the side of close described second roller of described screen cloth.
Preferably, described screen cloth is 0.5～1m to the distance of described conveyer belt.
Preferably, described screening plant also comprise under the bottom of being located at respectively described baffle plate and one end of close described second roller of described screen cloth under hopper.
Preferably, described power set are motor.
Preferably, described conveyer belt is belt.
Compared with correlation technique, the beneficial effects of the utility model are, effectively separate the powdered carbon in broken ferrophosphorus, reduce powdered carbon content in broken ferrophosphorus, improve ferrophosphorus burn-off rate, reduce power consumption, enhance productivity.
[brief description of the drawings]
Fig. 1 is the broken ferrophosphorus iron of the utility model charcoal separator structural representation.
[detailed description of the invention]
Below in conjunction with drawings and embodiments, the utility model is described in further detail.
As shown in Figure 1, the broken ferrophosphorus iron of the utility model charcoal separator comprises power set 3, the first roller 1, be positioned at the first roller 1 right side and with the first roller 1 the second roller 2 separated by a distance, be sheathed on the conveyer belt 5 outside the first roller 1 and the second roller 2 simultaneously and be located at the screening plant 9 under the first roller 1, power set 3 drive the first roller 1 and the second roller 2 interlock conveyer belt 5, the first roller 1 is permanent magnetism roller, this screening plant 9 comprises screen cloth 4 and is connected to the baffle plate 7 of screen cloth 4 bottoms, one end away from the second roller 2 of screen cloth 4 is positioned at the top near one end of the second roller 2, screen cloth 4 is provided with some through holes 41 that run through thereon, the aperture of through hole 41 is 3～5mm, the particle diameter of the aperture of this through hole 41 and the particle diameter of powdered carbon and ferrophosphorus powder adapts, use for powdered carbon particle and ferrophosphorus powder particles and pass through, screen cloth 4 is 40 °～60 ° with the angle of horizontal plane, baffle plate 7 is 1/5～2/5 of screen cloth 4 length to the distance of the side near the second roller 2 of screen cloth 4.
The broken ferrophosphorus material (not shown) that contains powdered carbon is to fall within conveyer belt 5 from feed opening 8, and moves towards the direction near the first roller 1 with conveyer belt 5.Because the first roller 1 has magnetic, ferrophosphorus is had to suction-operated, powdered carbon is not had to suction-operated, when material is during through the peak of the first roller 1, the impact of powdered carbon gravitate starts vertical drop, and ferrophosphorus is attached on conveyer belt 5 by the Adsorption Effect of the first roller 1 to continue to travel forward with conveyer belt 5, when ferrophosphorus is after the minimum point of the first roller 1, reduced gradually by the suction-operated of the first roller 1, just drop gradually on screen cloth 4 and along the incline direction landing of screen cloth 4, obviously, the position that the position that powdered carbon falls falls from ferrophosphorus is two different positions, effectively separate the powdered carbon in broken ferrophosphorus thereby realize, reduce powdered carbon content in broken ferrophosphorus, and then raising ferrophosphorus burn-off rate, reduce power consumption, enhance productivity.
In the time having powdered carbon particle to adhere on the ferrophosphorus powder particles in broken ferrophosphorus, powdered carbon particle can drop on screen cloth 4 with ferrophosphorus powder particles, after the through hole 41 of screen cloth 4, falls along baffle plate 7.When ferrophosphorus piece outside dephosphorization iron powder in broken ferrophosphorus falls within on screen cloth 4, tumble downwards along the incline direction of screen cloth 4.Obviously.The position, whereabouts that is stained with the ferrophosphorus powder particles of powdered carbon particle is different from the position, whereabouts of the ferrophosphorus piece in broken ferrophosphorus.Thus, can further realize the separation of powdered carbon in broken ferrophosphorus, more effectively reduce powdered carbon content in broken ferrophosphorus, and then improve ferrophosphorus burn-off rate, reduce power consumption, enhance productivity.
In present embodiment, feed opening 8 is to the distance h of conveyer belt 5
2be 1～3m, screen cloth 4 is to the distance h of conveyer belt 5
1be 0.5～1m, this screening plant 9 also comprise one end near the second roller 2 of being located at the first hopper 61 under baffle plate 7 bottoms and being positioned at screen cloth 4 under the second hopper 62, power set 3 are motor, conveyer belt 5 is belt.By the setting of aforementioned structure, can effectively realize separating and the collection respectively of broken ferrophosphorus and powdered carbon of broken ferrophosphorus and powdered carbon, and realize the continuous operation of this broken ferrophosphorus iron charcoal separator.
Compared with correlation technique, the beneficial effects of the utility model are, effectively separate the powdered carbon in broken ferrophosphorus, reduce powdered carbon content in broken ferrophosphorus, and then improve ferrophosphorus burn-off rate, reduce power consumption, enhance productivity.
Above-described is only embodiment of the present utility model; it should be pointed out that for the person of ordinary skill of the art at this, do not departing under the prerequisite of the utility model creation design; can also make improvement, but these all belong to protection domain of the present utility model.
Claims (5)
1. a broken ferrophosphorus iron charcoal separator, it is characterized in that: described broken ferrophosphorus iron charcoal separator comprises power set, the first roller, be positioned at described the first roller right side and with described the first roller the second roller separated by a distance, be sheathed on the conveyer belt outside described the first roller and described the second roller simultaneously and be located at the screening plant under described the first roller, described power set drive described the first roller and the second roller to rotate and interlock described in conveyer belt, described the first roller is permanent magnetism roller, described screening plant comprises screen cloth and is connected to the baffle plate of described screen bottom, one end away from described the second roller of described screen cloth is positioned at the top near one end of described the second roller, the aperture of described screen cloth is 3～5mm, the angle of described screen cloth and described horizontal plane is 40 °～60 °, described baffle plate is 1/5～2/5 of described screen cloth length to the distance of the side of close described second roller of described screen cloth.
2. broken ferrophosphorus iron charcoal separator according to claim 1, is characterized in that: described screen cloth is 0.5～1m to the distance of described conveyer belt.
3. broken ferrophosphorus iron charcoal separator according to claim 2, is characterized in that: described screening plant also comprise under the bottom of being located at respectively described baffle plate and one end of close described second roller of described screen cloth under hopper.
4. broken ferrophosphorus iron charcoal separator according to claim 3, is characterized in that: described power set are motor.
5. broken ferrophosphorus iron charcoal separator according to claim 4, is characterized in that: described conveyer belt is belt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420346714.3U CN203917157U (en) | 2014-06-26 | 2014-06-26 | Broken ferrophosphorus iron charcoal separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420346714.3U CN203917157U (en) | 2014-06-26 | 2014-06-26 | Broken ferrophosphorus iron charcoal separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203917157U true CN203917157U (en) | 2014-11-05 |
Family
ID=51813038
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420346714.3U Expired - Fee Related CN203917157U (en) | 2014-06-26 | 2014-06-26 | Broken ferrophosphorus iron charcoal separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203917157U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104646294A (en) * | 2015-02-05 | 2015-05-27 | 无为县环江铜业有限公司 | White copper particle sorting device |
-
2014
- 2014-06-26 CN CN201420346714.3U patent/CN203917157U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104646294A (en) * | 2015-02-05 | 2015-05-27 | 无为县环江铜业有限公司 | White copper particle sorting device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20141105 Termination date: 20160626 |