CN219334200U - Spherical nickel hydroxide continuous reaction kettle with solid content concentration and concentration device - Google Patents
Spherical nickel hydroxide continuous reaction kettle with solid content concentration and concentration device Download PDFInfo
- Publication number
- CN219334200U CN219334200U CN202320452843.XU CN202320452843U CN219334200U CN 219334200 U CN219334200 U CN 219334200U CN 202320452843 U CN202320452843 U CN 202320452843U CN 219334200 U CN219334200 U CN 219334200U
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- concentration
- reaction kettle
- nickel hydroxide
- solid content
- kettle body
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 41
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 title claims abstract description 17
- 239000007787 solid Substances 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 239000000463 material Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000036314 physical performance Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
The utility model discloses a spherical nickel hydroxide continuous reaction kettle with a solid content concentration device, which comprises: a reaction kettle body; the concentration component is arranged in the reaction kettle body; the clear liquid outlet is arranged on the upper side of the outer wall of the reaction kettle body and is communicated with the outlet end of the concentration component.
Description
Technical Field
The utility model relates to the technical field of continuous reaction kettles, in particular to a spherical nickel hydroxide continuous reaction kettle with a solid content concentration device.
Background
The spherical nickel hydroxide material has been developed into a mainstream battery anode material because of the advantages of good cycle performance, high specific capacity, high energy density and the like, and the solid content of slurry of the spherical nickel hydroxide material in the synthesis reaction process has an important influence on the physical performance of the spherical nickel hydroxide material, so that the reaction efficiency of the subsequent process can be effectively improved if the spherical nickel hydroxide material can undergo one-time concentration treatment during the synthesis reaction, however, the existing continuous reaction kettle does not have a concentration function, and the material needs to be taken out from the continuous reaction kettle and then is singly concentrated, thereby reducing the working efficiency, improving the labor cost and being not suitable for mass production operation.
Disclosure of Invention
Aiming at the technical problems, the utility model provides a spherical nickel hydroxide continuous reaction kettle with a solid content concentration device.
In order to achieve the above purpose, the technical scheme of the utility model is as follows:
a spherical nickel hydroxide continuous reaction kettle with a solid content concentration device comprises:
a reaction kettle body;
the concentration component is arranged in the reaction kettle body;
the clear liquid outlet is arranged on the upper side of the outer wall of the reaction kettle body and is communicated with the outlet end of the concentration component.
And the outlet end of the clarified liquid outlet is sequentially provided with a regulating valve and an external connection flowmeter.
The enrichment assembly includes:
the concentration tube is vertically arranged in the reaction kettle body, the bottom of the concentration tube is a liquid inlet, and the top of the concentration tube is a liquid outlet;
the inclined plates are alternately arranged in the concentration tube from top to bottom and left to right, so that an S-shaped liquid passage is formed in the concentration tube.
The liquid inlet and the liquid outlet of the concentration tube are both conical.
The utility model also comprises an overflow pipe which is vertically arranged in the reaction kettle body and positioned at the other side of the position of the clarified liquid outlet, and the outlet end of the overflow pipe is arranged at the top of the reaction kettle body.
The beneficial effects of the utility model are as follows: the utility model has simple structure and convenient operation, the concentration tube is matched with the inclined plate, and the material of the reaction kettle is effectively intercepted while the clear liquid of the reaction kettle is discharged, so that the solid content in the discharged wastewater is reduced, the concentration of the material in the reaction kettle is greatly improved, and the concentration is realized. The utility model can also adjust the physical and chemical properties and process indexes of the spherical nickel hydroxide, reduce the content of materials discharged into the wastewater, and realize economic and environmental benefits.
Drawings
Fig. 1 is a schematic structural view of the present utility model.
Detailed Description
The objects, technical solutions and advantages of the present utility model will become more apparent by the following detailed description of the present utility model with reference to the accompanying drawings. It should be understood that the description is only illustrative and is not intended to limit the scope of the utility model. In addition, in the following description, descriptions of well-known structures and techniques are omitted so as not to unnecessarily obscure the present utility model.
As shown in fig. 1, a spherical nickel hydroxide continuous reaction kettle with a solid content concentration device comprises: a reaction kettle body 1; the concentration component 2 is arranged in the reaction kettle body 1; the clarified liquid outlet 3 is arranged on the upper side of the outer wall of the reaction kettle body 1 and is communicated with the outlet end of the concentration component 2.
As shown in fig. 1, an outlet end of the clarified liquid outlet 3 is sequentially provided with a regulating valve 5 and an external connection flowmeter 4 for regulating the flow rate of the clarified liquid outlet.
As shown in fig. 1, the concentration assembly 2 includes: the concentration tube is vertically arranged in the reaction kettle body 1, the bottom of the concentration tube is a liquid inlet, and the top of the concentration tube is a liquid outlet; the inclined plates are alternately arranged in the concentration tube from top to bottom and left to right, so that an S-shaped liquid passage is formed in the concentration tube.
As shown in FIG. 1, the liquid inlet and the liquid outlet of the concentration tube are conical.
As shown in fig. 1, the utility model further comprises an overflow pipe 6 which is vertically arranged in the reaction kettle body 1 and positioned at the other side of the position of the clarified liquid outlet 3, the outlet end of the overflow pipe 6 is arranged at the top of the reaction kettle body 1, the outlet end of the overflow pipe 6 and the clarified liquid outlet 3 are arranged in a vertically staggered way, and the vertical liquid level difference exists to ensure the continuity of clarified liquid.
When the utility model is used, the suction pump is arranged at the outlet end of the external connection flowmeter 4, materials are injected into the reaction kettle body 1 to carry out synthesis reaction, then the materials in the kettle are pumped by the suction pump, the materials enter the pipe through the liquid inlet at the bottom of the concentration pipe and gradually rise in the S-shaped liquid-moving channel, in the process, heavy materials in liquid gradually sink on the inclined plate, so that the solution is gradually layered, the heavy materials gradually slide back into the reaction kettle body 1 along the inclined plate surface due to the action of gravity, namely, concentrated liquid descends, clarified liquid ascends, and the clarified solution is pumped out from the outlet 3 of the clarified liquid.
It is to be understood that the above-described embodiments of the present utility model are merely illustrative of or explanation of the principles of the present utility model and are in no way limiting of the utility model. Accordingly, any modification, equivalent replacement, improvement, etc. made without departing from the spirit and scope of the present utility model should be included in the scope of the present utility model. Furthermore, the appended claims are intended to cover all such changes and modifications that fall within the scope and boundary of the appended claims, or equivalents of such scope and boundary.
Claims (5)
1. The utility model provides a take spherical nickel hydroxide continuous reaction cauldron of concentrated enrichment facility of solid content which characterized in that includes:
a reaction kettle body (1);
the concentration component (2) is arranged in the reaction kettle body (1);
the clarifying solution outlet (3) is arranged on the upper side of the outer wall of the reaction kettle body (1) and is communicated with the outlet end of the concentration component (2).
2. The spherical nickel hydroxide continuous reaction kettle with the solid content concentration and concentration device according to claim 1, wherein an outlet end of the clarified liquid outlet (3) is sequentially provided with a regulating valve (5) and an external connection flowmeter (4).
3. The spherical nickel hydroxide continuous reactor with a solid content concentration and concentration device according to claim 1, wherein the concentration assembly (2) comprises:
the concentration tube is vertically arranged in the reaction kettle body (1), the bottom of the concentration tube is a liquid inlet, and the top of the concentration tube is a liquid outlet;
the inclined plates are alternately arranged in the concentration tube from top to bottom and left to right, so that an S-shaped liquid passage is formed in the concentration tube.
4. The spherical nickel hydroxide continuous reaction kettle with the solid content concentration and concentration device according to claim 3, wherein the liquid inlet and the liquid outlet of the concentration tube are conical.
5. The spherical nickel hydroxide continuous reaction kettle with the solid content concentration and concentration device according to claim 1, further comprising an overflow pipe (6) vertically arranged in the reaction kettle body (1) and positioned at the other side of the position of the clarified liquid outlet (3), wherein the outlet end of the overflow pipe is arranged at the top of the reaction kettle body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320452843.XU CN219334200U (en) | 2023-03-11 | 2023-03-11 | Spherical nickel hydroxide continuous reaction kettle with solid content concentration and concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320452843.XU CN219334200U (en) | 2023-03-11 | 2023-03-11 | Spherical nickel hydroxide continuous reaction kettle with solid content concentration and concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219334200U true CN219334200U (en) | 2023-07-14 |
Family
ID=87101844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320452843.XU Active CN219334200U (en) | 2023-03-11 | 2023-03-11 | Spherical nickel hydroxide continuous reaction kettle with solid content concentration and concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219334200U (en) |
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2023
- 2023-03-11 CN CN202320452843.XU patent/CN219334200U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240227 Address after: 737100 No. 2 Lanzhou Road, Beijing Road Street, Jinchuan District, Jinchang City, Gansu Province Patentee after: Jinchuan Group Nickel Cobalt Co.,Ltd. Country or region after: China Address before: 737103 No. 98, Jinchuan Road, Jinchang, Gansu Patentee before: JINCHUAN GROUP Co.,Ltd. Country or region before: China |
|
| TR01 | Transfer of patent right |