CN207046881U - A kind of preparation facilities of low sodium cobaltosic oxide - Google Patents
A kind of preparation facilities of low sodium cobaltosic oxide Download PDFInfo
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- CN207046881U CN207046881U CN201720532540.3U CN201720532540U CN207046881U CN 207046881 U CN207046881 U CN 207046881U CN 201720532540 U CN201720532540 U CN 201720532540U CN 207046881 U CN207046881 U CN 207046881U
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- centrifuge
- pipeline
- cobaltosic oxide
- mixing machine
- preparation facilities
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Abstract
The utility model discloses a kind of preparation facilities of low sodium cobaltosic oxide, it includes reactive tank, the first centrifuge, pushed bat kiln, aging reactor, the second centrifuge, drier, mixing machine, and the reactive tank, the first centrifuge, pushed bat kiln, aging reactor, the second centrifuge, drier and mixing machine pass sequentially through pipeline and be connected.The utility model is when in use, the cobaltosic oxide being prepared passes sequentially through the first centrifuge, pushed bat kiln, aging reactor, the second centrifuge, drier, mixing machine by pipeline, when carrying out a centrifuge washing, ageing and secondary centrifuging washing to cobaltosic oxide, the inlet of water is controlled by flow controller, so as to avoid the waste of water resource；By setting pushed bat kiln, realize and calcination is carried out to cobaltosic oxide, make sodium become easily to flow；By setting the second centrifuge so that sodium ion is thoroughly washed off, cumbersome so as to solve apparatus structure imperfection in the prior art, obtains the problem of sodium content is high.
Description
Technical field
The utility model belongs to the preparation facilities technical field of cobaltosic oxide, and in particular to a kind of low sodium cobaltosic oxide
Preparation facilities.
Background technology
In the generating process of cobaltosic oxide, spherical cobalt forms specified size, and main environment material is sodium salt, growth
Meanwhile the sodium salt of certain content is progressively included, and the structure of ball cobalt is porous, specific surface area is the index of its porous measurement,
When centrifuge washs, sodium content exponentially level declines, and it is poorer more to arrive clean result below, to reach below acceptance value, often needs
Want more hot water, and longer wash time；And it is current each cobalt acid lithium factory necessary to improving quality to reduce sodium
House, to determining that unwanted impurity requirement is also improving constantly in cobaltosic oxide, but existing prepare low sodium cobaltosic oxide
Device it is simpler, therefore hardly result in the relatively low cobaltosic oxide of sodium content.
Utility model content
In view of this, main purpose of the present utility model is to provide a kind of preparation facilities of low sodium cobaltosic oxide, solution
Certainly apparatus structure imperfection in the prior art, it is cumbersome the problem of.
To reach above-mentioned purpose, what the technical solution of the utility model was realized in：A kind of low sodium cobaltosic oxide
Preparation facilities, it includes reactive tank, the first centrifuge, pushed bat kiln, aging reactor, the second centrifuge, drier, mixing machine, described
Reactive tank, the first centrifuge, pushed bat kiln, aging reactor, the second centrifuge, drier and mixing machine pass sequentially through pipeline and are connected
It is logical.
Preferably, in addition to filter tunnel and cell body, the filter tunnel are arranged at the discharge outlet of reactive tank lower end, institute
State the lower section that cell body is arranged at filter tunnel, the bottom of the cell body is provided with discharge gate, the discharge gate by pipeline with from
The charging aperture of scheming upper end is connected.
Preferably, first centrifuge, aging reactor, be respectively arranged with the first water inlet, at the top of the second centrifuge
Two water inlets, the 3rd water inlet, first water inlet, the second water inlet, the 3rd water inlet pass through pipeline and water system
It is connected, flow control valve is provided with the pipeline being connected with water system.
Preferably, it also includes folding type packaging bag, has and mixing machine top discharge mouth phase on the folding type packaging bag
The tightening device of cooperation.
Preferably, the pipeline that the pipeline and aging reactor that the cell body is connected with the first centrifuge are connected with the second centrifuge
On be provided with pump and control valve；On the pipeline that first centrifuge is connected with pushed bat kiln, pushed bat kiln and aging reactor connection
Control is provided with pipeline, on the pipeline that the second centrifuge is connected with drier and on pipeline that drier is connected with mixing machine
Valve.
Preferably, the discharge outlet of the mixing machine lower end is provided with butterfly switch.
Compared with prior art, the utility model when in use, the cobaltosic oxide being prepared by pipeline successively
By the first centrifuge, pushed bat kiln, aging reactor, the second centrifuge, drier, mixing machine, wherein, carried out to cobaltosic oxide
When centrifuge washing, ageing and secondary centrifuging are washed, the inlet of water is controlled by flow controller, so as to avoid water
The waste of resource；By setting pushed bat kiln, realize and calcination is carried out to cobaltosic oxide, make sodium become easily to flow；By setting the
Two centrifuges so that sodium ion is thoroughly washed off, cumbersome so as to solve apparatus structure imperfection in the prior art,
Obtain the problem of sodium content is high.
Brief description of the drawings
Fig. 1 is a kind of structural representation of the preparation facilities of low sodium cobaltosic oxide of the utility model.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining
The utility model, it is not used to limit the utility model.
The utility model provides a kind of preparation facilities of low sodium cobaltosic oxide, as shown in figure 1, it include reactive tank 1,
First centrifuge 2, pushed bat kiln 3, aging reactor 4, the second centrifuge 5, drier 6, mixing machine 7, reactive tank 1, the first centrifuge 2,
Pushed bat kiln 3, aging reactor 4, the second centrifuge 5, drier 6 and mixing machine 7 pass sequentially through pipeline and are connected.
Further, in addition to filter tunnel 11 and cell body 12, filter tunnel 11 are arranged at the discharging of the lower end of reactive tank 1
At mouthful, cell body 12 is arranged at the lower section of filter tunnel 11, and the bottom of cell body 12 is provided with discharge gate 121, and discharge gate 121 passes through pipe
Road is connected with the charging aperture of centrifuge upper end.
Further, the first centrifuge 2, aging reactor 4, the top of the second centrifuge 6 be respectively arranged with the first water inlet 21,
Second water inlet 41, the 3rd water inlet 51, the first water inlet 21, the second water inlet 41, the 3rd water inlet 51 by pipeline with
Water system 8 is connected, and flow control valve is provided with the pipeline being connected with water system 8.
Further, it also includes folding type packaging bag 9, has and the top discharge mouth of mixing machine 7 on folding type packaging bag 9
The tightening device 91 being engaged.
Further, what the pipeline and aging reactor 4 that cell body 12 is connected with the first centrifuge 2 were connected with the second centrifuge 5
Pump and control valve are provided with pipeline；On the pipeline that first centrifuge 2 is connected with pushed bat kiln 3, pushed bat kiln 3 connects with aging reactor 4
Set on the pipeline connect, on the pipeline that the second centrifuge 5 is connected with drier 6 and on pipeline that drier 6 is connected with mixing machine 7
It is equipped with control valve.
Further, the discharge outlet of the lower end of mixing machine 7 is provided with butterfly switch 71.
The utility model when in use, the cobaltosic oxide being prepared by pipeline pass sequentially through the first centrifuge,
Pushed bat kiln, aging reactor, the second centrifuge, drier, mixing machine, wherein, a centrifuge washing, old is being carried out to cobaltosic oxide
When change and secondary centrifuging are washed, the inlet of water is controlled by flow controller, so as to avoid the waste of water resource；Pass through
Pushed bat kiln is set, realizes and calcination is carried out to cobaltosic oxide, make sodium become easily to flow；By setting the second centrifuge so that sodium
Ion is thoroughly washed off, cumbersome so as to solve apparatus structure imperfection in the prior art, obtains that sodium content is high to ask
Topic
It is described above, preferred embodiment only of the present utility model, it is not intended to limit protection of the present utility model
Scope.
Claims (6)
1. a kind of preparation facilities of low sodium cobaltosic oxide, it is characterised in that it includes reactive tank (1), the first centrifuge, push pedal
Kiln, aging reactor, the second centrifuge, drier, mixing machine, the reactive tank, the first centrifuge, pushed bat kiln, aging reactor, second from
Scheming, drier and mixing machine pass sequentially through pipeline and are connected.
2. the preparation facilities of a kind of low sodium cobaltosic oxide according to claim 1, it is characterised in that also include filtering leakage
Bucket and cell body, the filter tunnel are arranged at the discharge outlet of reactive tank lower end, and the cell body is arranged at the lower section of filter tunnel,
The bottom of the cell body is provided with discharge gate, and the discharge gate is connected by pipeline with the charging aperture of centrifuge upper end.
A kind of 3. preparation facilities of low sodium cobaltosic oxide according to claim 2, it is characterised in that first centrifugation
Machine, aging reactor, it is respectively arranged with the first water inlet, the second water inlet, the 3rd water inlet at the top of the second centrifuge, described first
Water inlet, the second water inlet, the 3rd water inlet be connected by pipeline with water system, described to be connected with water system
Flow control valve is provided with pipeline.
4. the preparation facilities of a kind of low sodium cobaltosic oxide according to claim 3, it is characterised in that it also includes folding
Formula packaging bag, there is the tightening device being engaged with mixing machine top discharge mouth on the folding type packaging bag.
5. the preparation facilities of a kind of low sodium cobaltosic oxide according to claim 4, it is characterised in that the cell body and
Pump and control valve are provided with the pipeline that the pipeline and aging reactor of one centrifuge connection are connected with the second centrifuge；Described
On the pipeline that one centrifuge is connected with pushed bat kiln, on the pipeline of pushed bat kiln and aging reactor connection, the second centrifuge and drier company
Control valve is provided with the pipeline connect and on pipeline that drier is connected with mixing machine.
6. the preparation facilities of a kind of low sodium cobaltosic oxide according to claim 4, it is characterised in that under the mixing machine
The discharge outlet at end is provided with butterfly switch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720532540.3U CN207046881U (en) | 2017-05-15 | 2017-05-15 | A kind of preparation facilities of low sodium cobaltosic oxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720532540.3U CN207046881U (en) | 2017-05-15 | 2017-05-15 | A kind of preparation facilities of low sodium cobaltosic oxide |
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| Publication Number | Publication Date |
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| CN207046881U true CN207046881U (en) | 2018-02-27 |
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| CN201720532540.3U Active CN207046881U (en) | 2017-05-15 | 2017-05-15 | A kind of preparation facilities of low sodium cobaltosic oxide |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112645393A (en) * | 2020-12-21 | 2021-04-13 | 格林美（江苏）钴业股份有限公司 | Preparation method of cobaltosic oxide |
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2017
- 2017-05-15 CN CN201720532540.3U patent/CN207046881U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112645393A (en) * | 2020-12-21 | 2021-04-13 | 格林美（江苏）钴业股份有限公司 | Preparation method of cobaltosic oxide |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 225400 Taixing Economic Development Zone, Jiangsu, Binjiang, North Road, No. 8, No. Patentee after: Grammy (Jiangsu) cobalt industry Limited by Share Ltd Address before: 225400 Taixing Economic Development Zone, Jiangsu, Binjiang, North Road, No. 8, No. Patentee before: Jiangsu Cobalt Nickel Metal Co., Ltd. |