CN205642057U - A granulation formula rotary kiln for calcining electrolytic manganese slag - Google Patents
A granulation formula rotary kiln for calcining electrolytic manganese slag Download PDFInfo
- Publication number
- CN205642057U CN205642057U CN201620355018.8U CN201620355018U CN205642057U CN 205642057 U CN205642057 U CN 205642057U CN 201620355018 U CN201620355018 U CN 201620355018U CN 205642057 U CN205642057 U CN 205642057U
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- CN
- China
- Prior art keywords
- chain
- rotary kiln
- electrolytic manganese
- hangers
- manganese slag
- 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.)
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Abstract
The utility model particularly relates to a rotary kiln for calcining electrolytic manganese slag. The utility model aims to provide a can make the granule with electrolytic manganese slag in calcination process, make things convenient for a granulation formula rotary kiln for calcining electrolytic manganese slag of later stage processing, include along the chain of rotary kiln axis setting, the both ends of chain all hang on the rotary kiln inner wall through the hangers, two suspension end's on the chain distance is less than the length of chain, chain symmetry in pairs sets up the both sides at the rotary kiln axis, the line that the both sides chain corresponds the hangers is all on the diameter of rotary kiln. The utility model provides a chain is along the axis setting of rotary kiln, and the chain can carry out the whipping along with the rotary motion of rotary kiln, and the whipping in -process can hit sticky electrolytic manganese slag and beat, because chain itself has a hole, beats the in -process hitting, thereby receives extrusion granulation form from the electrolytic manganese slag that the chain passed, makes things convenient for the later stage to grind processing, the especially processing of the super powder.
Description
Technical field
This utility model belongs to rotary kiln technical field, is specifically related to a kind of useless for calcining electrolytic manganese
The rotary kiln of slag.
Background technology
Electrolytic manganese waste residue is the industrial residue of discharge in electrolytic manganese smelt production, and its character is
The viscosity cake of the moisture content about 27%-28% that 90 mesh fine powders are formed.Electrolytic manganese waste residue contains
Substantial amounts of building materials desired substance, the electrolytic manganese waste residue after high-temperature calcination can replace natural stone
Cream, desulfurated plaster are as the retarder of cement, it is also possible to be ground being processed into superfine again and be allocated as
For the external feeding of commerical ready-mixed concrete, replace super finely ground slag, flyash etc..Electrolytic manganese residues is at rotary kiln
In calcining be generally divided into owing to the recycling of electrolytic manganese waste residue is a kind of emerging green technology,
Prior art does not adapt to the calcining rotary furnace of electrolytic manganese waste residue character.Use in prior art
Rotary furnace the electrolytic manganese waste residue of viscosity pie is directly calcined, form the group of bulk after calcining
Shape, owing to volume is relatively big, causes greatly puzzlement to the attrition process in later stage, needs repeatedly to grind
Mill could prepare super fine, and labor intensity is higher, inefficiency.
Utility model content
The purpose of this utility model is to provide a kind of pelletize formula revolution for calcining electrolytic manganese waste residue
Kiln, it is possible in calcination process, electrolytic manganese waste residue is made granule, facilitates post-production.
For achieving the above object, this utility model be the technical scheme is that for calcining
The pelletize formula rotary kiln of electrolytic manganese waste residue, including the chain arranged along rotary kiln axis；Described chain
Two ends be all suspended on rotary kiln inwall；The distance of described chain two suspended end is less than the length of chain
Degree.
Preferred: described chain is hung by the hangers being welded on rotary kiln inwall；Described
Hangers is semicircular ring, is connected by chain ring between described hangers and chain.
Preferred: described chain is symmetricly set on the both sides of rotary kiln axis, described two side chains in pairs
The line of bar correspondence hangers is all at rotary kiln diametrically.
Preferably, in described rotary kiln, it is provided with two pairs of unequal chains of length, and short chain
Two hangers are arranged between two hangers of reel chain.
Preferably, described chain is the high-tensile round-link chain of Carburization Treatment.
This utility model has the advantages that the distance of described chain two suspended end is less than chain
Length so that chain can keep lax state；Chain is arranged along the axis of rotary kiln, chain
Bar can carry out whipping along with the rotary motion of rotary kiln, can give up the electrolytic manganese of viscosity during whipping
Slag impacts, owing to chain itself has hole, in shots, and the electricity passed from chain
Solution manganese waste slag is squeezed thus forms graininess, facilitates later stage attrition process, particularly micropowder
Processing.
Accompanying drawing explanation
Fig. 1 is the structural representation of embodiment 1；
Fig. 2 is the structural representation of embodiment 2.
Detailed description of the invention
Embodiment 1
As shown in Figure 1, for calcining the pelletize formula rotary kiln of electrolytic manganese waste residue, including along revolution
The chain 1 that kiln axis is arranged, chain 1 can carry out whipping, whipping along with the rotary motion of rotary kiln
During the electrolytic manganese waste residue of viscosity can be impacted, owing to chain 1 itself has hole,
In shots, the electrolytic manganese waste residue passed from chain 1 is squeezed thus forms graininess.Institute
The two ends stating chain 1 are all suspended on rotary kiln inwall, and the distance of described 1 liang of suspended end of chain is little
Length in chain 1 so that chain 1 can keep lax state.Described chain 1 is by weldering
The hangers 2 being connected on rotary kiln inwall hangs；Described hangers 2 is semicircular ring, described hangers
Being connected by chain ring between 2 with chain 1, chain ring can open and close, and conveniently carries out chain
The installation of bar 1 and replacing.Described chain 1 is symmetricly set on the both sides of rotary kiln axis in pairs,
Be arranged in rotary kiln to chain 1 can be greatly improved the work efficiency of rotary kiln；Described two side chains
All at rotary kiln cross section diametrically, such setting can be maximum for the line of the corresponding hangers 2 of bar 1
Limit improves the impulse stroke of chain 1.Being provided with a pair chain 1 in the present embodiment, this is to chain
The position height of 1 can change along with the rotation of rotary kiln, and one of them chain 1 rises, the most separately
One chain 1 declines, and potential energy is kinetic energy during declining by chain 1, thus by electrolytic manganese
Waste residue impacts into granule, facilitates the processing of later stage attrition process, particularly micropowder.Described chain
1 is the high-tensile round-link chain of Carburization Treatment, improves intensity and the anti-wear performance of chain 1.
Embodiment 2
With embodiment 1 except that, as in figure 2 it is shown, the present embodiment is provided with two pairs of chains:
Two pairs of unequal chains of length, and two hangers 2 of short chain 4 it are provided with in described rotary kiln
It is arranged between two hangers 2 of reel chain 3, is so avoided that reel chain 3 and short chain 4
It is wound around during working at the same time；Meanwhile, for embodiment 1, two are arranged right
The work efficiency of rotary kiln can be doubled by chain.
Although this utility model only lists a pair chain and the embodiment of two pairs of chains, but uses
It is new that the technical scheme of more than the two pairs chain same or like technique effects of acquisition still falls within this practicality
In the protection domain of type.
Claims (5)
1. for calcining the pelletize formula rotary kiln of electrolytic manganese waste residue, it is characterised in that: include along returning
The chain that rotary kiln axis is arranged；The two ends of described chain are all suspended on rotary kiln inwall；Described chain
The distance of bar two suspended end is less than the length of chain.
Pelletize formula rotary kiln for calcining electrolytic manganese waste residue the most according to claim 1,
Its spy is: described chain is hung by the hangers being welded on rotary kiln inwall；Described extension
Ear is semicircular ring, is connected by chain ring between described hangers and chain.
Pelletize formula rotary kiln for calcining electrolytic manganese waste residue the most according to claim 2,
Its spy is: described chain is symmetricly set on the both sides of rotary kiln axis, described both sides chain in pairs
The line of corresponding hangers is all at rotary kiln cross section diametrically.
Pelletize formula rotary kiln for calcining electrolytic manganese waste residue the most according to claim 3,
Its spy is: be provided with two pairs of unequal chains of length, and the two of short chain in described rotary kiln
Individual hangers is arranged between two hangers of reel chain.
5. according to the described pelletize for calcining electrolytic manganese waste residue arbitrary in Claims 1-4
Formula rotary kiln, its spy is: described chain is the high-tensile round-link chain of Carburization Treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620355018.8U CN205642057U (en) | 2016-04-25 | 2016-04-25 | A granulation formula rotary kiln for calcining electrolytic manganese slag |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620355018.8U CN205642057U (en) | 2016-04-25 | 2016-04-25 | A granulation formula rotary kiln for calcining electrolytic manganese slag |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205642057U true CN205642057U (en) | 2016-10-12 |
Family
ID=57062954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620355018.8U Expired - Fee Related CN205642057U (en) | 2016-04-25 | 2016-04-25 | A granulation formula rotary kiln for calcining electrolytic manganese slag |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205642057U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110357130A (en) * | 2019-08-07 | 2019-10-22 | 葫芦岛虹京科技有限公司 | A kind of acidizing fired device and its production method improving lithium carbonate conversion ratio |
-
2016
- 2016-04-25 CN CN201620355018.8U patent/CN205642057U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110357130A (en) * | 2019-08-07 | 2019-10-22 | 葫芦岛虹京科技有限公司 | A kind of acidizing fired device and its production method improving lithium carbonate conversion ratio |
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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: 20161012 Termination date: 20210425 |