CN204911484U - Cobaltous carbonate is reaction unit of synthesis in succession - Google Patents
Cobaltous carbonate is reaction unit of synthesis in succession Download PDFInfo
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- CN204911484U CN204911484U CN201520480256.7U CN201520480256U CN204911484U CN 204911484 U CN204911484 U CN 204911484U CN 201520480256 U CN201520480256 U CN 201520480256U CN 204911484 U CN204911484 U CN 204911484U
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- reaction
- bypass channel
- cobaltous carbonate
- pannikin
- pump
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Abstract
The utility model discloses a cobaltous carbonate is reaction unit of synthesis in succession. It includes reaction still and bypass channel, is equipped with the closed lower extreme open -ended water knockout drum in upper end in bypass channel the reaction still in be equipped with the little pot of reaction, little pot upper end opening react, the lower extreme seals, is equipped with the agitator in the little pot of reaction, is equipped with the drainage tube on the lateral wall upper portion of reaction still, the other end of drainage tube passes during bypass channel stretches into the water knockout drum, the bypass channel lower extreme is equipped with the bin outlet, the bin outlet manage say with the entry linkage of pump, delivery side of pump and another pipe connection, the other end of this pipeline stretches into and reacts in little pot bypass channel lateral wall upper portion be equipped with the drain pipe. The utility model discloses the defect that the increase that can avoid the continuous building -up process aqueous phase of cobaltous carbonate caused the granularity appearance of cobaltous carbonate to reach the requirement has realized going on in succession of cobaltous carbonate building -up reactions to the dynamics appearance all reaches the requirement.
Description
Technical field:
The utility model belongs to chemical field, is specifically related to a kind of reaction unit of cobalt carbonate continuous synthesis.
Background technology:
In the synthetic reaction process of cobalt carbonate, in order to reach the requirement of granularity pattern, synthetic reaction for a long time must be carried out continuously, but in course of reaction, along with the continuous increase of aqueous phase, granularity pattern is difficult to reach requirement, and some aqueous phase must be divided could to continue reaction.
Summary of the invention:
The purpose of this utility model be to provide one can and the time-division remove some aqueous phase, the synthetic reaction of cobalt carbonate is well carried out for a long time, thus makes the granularity pattern of cobalt carbonate meet the requirements of the reaction unit of cobalt carbonate continuous synthesis.
The utility model is implemented by the following technical programs:
The reaction unit of cobalt carbonate continuous synthesis of the present utility model, it is characterized in that, comprise reaction pot and bypass channel, the water knockout drum of upper end closed lower ending opening is provided with in bypass channel, reaction pannikin is provided with in described reaction pot, reaction pannikin upper end open, lower end closed, agitator is provided with in reaction pannikin, drainage tube is provided with in the side wall upper part of reaction pot, the other end of drainage tube stretches in water knockout drum through bypass channel, bypass channel lower end is provided with discharge gate, discharge gate is connected with the entrance of pump through pipeline, delivery side of pump is connected with another pipeline, the other end of this pipeline stretches in reaction pannikin, drainpipe is provided with in described bypass channel side wall upper part.
The reaction unit of cobalt carbonate continuous synthesis of the present utility model runs like this: the synthetic reaction of cobalt carbonate is carried out in reaction pannikin, agitator limit in reaction pannikin is stirred, the material by reaction pot wall outside reaction pannikin and water liquid do not rotate with the stirring in reaction pannikin and acutely overturn, static current are introduced in water knockout drum through drainage tube, material precipitates in water knockout drum, solid falls into the bottom of bypass channel, through discharge gate, pump and pipeline flow in reaction pannikin, and the aqueous phase in bypass channel is discharged through drainpipe, the increase of cobalt carbonate continuous synthesis process aqueous phase can be avoided thus to cause the granularity pattern of cobalt carbonate to meet the requirements of defect, achieve carrying out continuously of cobalt carbonate synthetic reaction, and dynamics pattern all reaches requirement.
Accompanying drawing illustrates:
Fig. 1 is the structural representation of the reaction unit of cobalt carbonate continuous synthesis of the present utility model;
Wherein 1, reaction pot; 2, bypass channel; 3, pannikin is reacted; 4, agitator; 5, drainage tube; 6, water knockout drum; 7, drainpipe; 8, discharge gate; 9, pump.
Detailed description of the invention:
Following examples further illustrate of the present utility model, instead of to restriction of the present utility model.
Embodiment 1:
As shown in Figure 1, the reaction unit of the cobalt carbonate continuous synthesis of the present embodiment, comprise reaction pot 1 and bypass channel 2, the water knockout drum 6 of upper end closed lower ending opening is provided with in bypass channel, reaction pannikin 3 is provided with in described reaction pot, reaction pannikin upper end open, lower end closed, agitator 4 is provided with in reaction pannikin, drainage tube 5 is provided with in the side wall upper part of reaction pot, the other end of drainage tube stretches in water knockout drum 6 through bypass channel 2, bypass channel lower end is provided with discharge gate 8, discharge gate is connected through the entrance of pipeline with pump 9, delivery side of pump is connected with another pipeline, the other end of this pipeline stretches in reaction pannikin 3, drainpipe 7 is provided with in described bypass channel 2 side wall upper part.
Claims (1)
1. the reaction unit of a cobalt carbonate continuous synthesis, it is characterized in that, comprise reaction pot and bypass channel, the water knockout drum of upper end closed lower ending opening is provided with in bypass channel, reaction pannikin is provided with in described reaction pot, reaction pannikin upper end open, lower end closed, agitator is provided with in reaction pannikin, drainage tube is provided with in the side wall upper part of reaction pot, the other end of drainage tube stretches in water knockout drum through bypass channel, bypass channel lower end is provided with discharge gate, discharge gate is connected with the entrance of pump through pipeline, delivery side of pump is connected with another pipeline, the other end of this pipeline stretches in reaction pannikin, drainpipe is provided with in described bypass channel side wall upper part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520480256.7U CN204911484U (en) | 2015-07-02 | 2015-07-02 | Cobaltous carbonate is reaction unit of synthesis in succession |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520480256.7U CN204911484U (en) | 2015-07-02 | 2015-07-02 | Cobaltous carbonate is reaction unit of synthesis in succession |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204911484U true CN204911484U (en) | 2015-12-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520480256.7U Active CN204911484U (en) | 2015-07-02 | 2015-07-02 | Cobaltous carbonate is reaction unit of synthesis in succession |
Country Status (1)
| Country | Link |
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| CN (1) | CN204911484U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110589900A (en) * | 2019-10-11 | 2019-12-20 | 合肥融捷金属科技有限公司 | Spherical cobalt carbonate production equipment and operation method thereof |
-
2015
- 2015-07-02 CN CN201520480256.7U patent/CN204911484U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110589900A (en) * | 2019-10-11 | 2019-12-20 | 合肥融捷金属科技有限公司 | Spherical cobalt carbonate production equipment and operation method thereof |
| CN110589900B (en) * | 2019-10-11 | 2021-11-16 | 合肥融捷金属科技有限公司 | Spherical cobalt carbonate production equipment and operation method thereof |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: Xishanlingjiao, Mashui Town, Yangchun City, Yangjiang City, Guangdong Province 529500 Patentee after: Kelixin (Yangjiang) new energy Co.,Ltd. Address before: 529625 Xishan Lingjiao, Mashui Town, Yangchun City, Yangjiang City, Guangdong Province Patentee before: YANGJIANG FEDERATION METAL CHEMICAL CO.,LTD. |