CN202322408U - Multi-barrel continuous liquid leaching equipment for preparing manganese sulfate solution - Google Patents
Multi-barrel continuous liquid leaching equipment for preparing manganese sulfate solution Download PDFInfo
- Publication number
- CN202322408U CN202322408U CN2011203681853U CN201120368185U CN202322408U CN 202322408 U CN202322408 U CN 202322408U CN 2011203681853 U CN2011203681853 U CN 2011203681853U CN 201120368185 U CN201120368185 U CN 201120368185U CN 202322408 U CN202322408 U CN 202322408U
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- CN
- China
- Prior art keywords
- leaching
- barrel
- drainage tube
- sulfate solution
- manganese sulfate
- 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.)
- Expired - Fee Related
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Abstract
The utility model discloses multi-barrel continuous liquid leaching equipment for preparing a manganese sulfate solution, which is characterized in that a water inlet hole (1) is arranged at one end of a leaching barrel I (1A); the other end of the leaching barrel I (1A) is provided with a drainage tube I (3A), and a blender I (2A) is arranged above the leaching barrel I (1A); an outlet of the drainage tube I (3A) is continuously connected with a leaching barrel II (1B), the other end of the leaching barrel II (1B) is provided with a drainage tube II (3B), and a blender II (2B) is arranged above the leaching barrel II (1B); and a multistage liquid leaching process equipment is formed through such reciprocation. The utility model aims to provide equipment for leaching ore pulp by stages in a plurality of leaching barrels and enabling the ore pulp to continuously react in the plurality of leaching barrels.
Description
Technical field
The utility model relates to preparation manganese sulfate solution field, relates in particular to many barrels of continuous leach liquor equipment of preparation manganese sulfate solution.
Background technology
Present single barrel of extract technology generally using of preparation manganese sulfate solution, whole leaching process is accomplished in single leaching bucket, its ore pulp contain sour passing in time; The reaction of ore pulp is leached and is reduced; Sluggish sedimentation breeze can not get relatively stable acidiferous long-term leaching, and its sedimentation breeze manganese slag contains soluble manganese and reaches 8%-18%, feeds intake for discontinuity in addition; Extended and leached the time that recycles of bucket, waste Mineral resources and the efficient that has reduced equipment.
The utility model content
The purpose of the utility model provides a kind of ore pulp and is leached by the segmentation of a plurality of leaching bucket, and the equipment of ore pulp successive reaction in a plurality of leaching buckets.
In order to realize above purpose, the technical scheme that the utility model adopts: a kind of many barrels of continuous leach liquor equipment that prepare manganese sulfate solution is characterized in that prosopyle (1) is arranged on an end of leaching bucket I (1A); The other end of leaching bucket I (1A) is equipped with drainage tube I (3A), and leaching bucket I (1A) top is equipped with stirrer I (2A); The outlet of drainage tube I (3A) continues to connect leaching bucket II (1B), and the other end of leaching bucket II (1B) is equipped with drainage tube II (3B), and leaching bucket II (1B) top is equipped with stirrer II (2B); So back and forth form multistage leach liquor processing unit.
The beneficial effect of the utility model: the utility model adopts many barrels of continuous leach liquor equipment, after leaching piecemeal, effectively raises the leaching yield and the dried slag rate that reduces the terminal point leached mud of breeze.Owing to adopt many barrels of continuous leach liquor equipment, possessing in the leaching bucket has metastable scope to contain acid, has accelerated the speed of response of ore pulp, has improved the leaching yield of plant efficiency and breeze, the leaching bucket under the equal scale, and yield-power is 2 times of single barrel of extract technology.
Description of drawings
Fig. 1 is the connection synoptic diagram of the utility model.
Each numerical reference is expressed as in the drawings, and 1, the prosopyle; 1A, leaching bucket I; 2A, stirrer I; 3A, drainage tube I; 1B, leaching bucket II; 2B, stirrer II; 3B, drainage tube II.
Embodiment
As shown in Figure 1, the assembly relation of the utility model is: prosopyle 1 is arranged on the end of leaching bucket I 1A; The other end of leaching bucket I 1A is equipped with drainage tube I 3A, and leaching bucket I 1A top is equipped with stirrer I 2A; The outlet of drainage tube I 3A continues to connect leaching bucket II 1B, and the other end of leaching bucket II 1B is equipped with drainage tube II 3B, and leaching bucket II 1B top is equipped with stirrer II 2B; So back and forth form multistage leach liquor processing unit.
As shown in Figure 1, the principle of work of the utility model: at first in leaching bucket I 1A, add the manganese ore powder, and add concentrated sulfuric acid solution through inlet opening 1, stirrer I 2A work makes the vitriol oil and manganese ore powdered reaction even simultaneously.The solution that has reacted gets into leaching bucket II 1B through drainage tube I 3A, and stirrer II 2B work simultaneously makes solution further reaction in leaching bucket II 1B, makes that the manganese element in the manganese ore further becomes manganese sulfate solution.The solution that has reacted gets into next stage leaching bucket through drainage tube II 3B, and so back and forth, the vitriol oil and manganese ore powder react in the multilevel leaching bucket, finally obtain the higher manganese sulfate solution of concentration.
Claims (1)
1. many barrels of continuous leach liquor equipment that prepare manganese sulfate solution is characterized in that prosopyle (1) is arranged on an end of leaching bucket I (1A); The other end of leaching bucket I (1A) is equipped with drainage tube I (3A), and leaching bucket I (1A) top is equipped with stirrer I (2A); The outlet of drainage tube I (3A) continues to connect leaching bucket II (1B), and the other end of leaching bucket II (1B) is equipped with drainage tube II (3B), and leaching bucket II (1B) top is equipped with stirrer II (2B); So back and forth form multistage leach liquor processing unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203681853U CN202322408U (en) | 2011-09-29 | 2011-09-29 | Multi-barrel continuous liquid leaching equipment for preparing manganese sulfate solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203681853U CN202322408U (en) | 2011-09-29 | 2011-09-29 | Multi-barrel continuous liquid leaching equipment for preparing manganese sulfate solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202322408U true CN202322408U (en) | 2012-07-11 |
Family
ID=46434398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203681853U Expired - Fee Related CN202322408U (en) | 2011-09-29 | 2011-09-29 | Multi-barrel continuous liquid leaching equipment for preparing manganese sulfate solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202322408U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105420493A (en) * | 2015-12-28 | 2016-03-23 | 云南云铜锌业股份有限公司 | Wet-metallurgy continuous reaction kettle equipment |
-
2011
- 2011-09-29 CN CN2011203681853U patent/CN202322408U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105420493A (en) * | 2015-12-28 | 2016-03-23 | 云南云铜锌业股份有限公司 | Wet-metallurgy continuous reaction kettle equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120711 Termination date: 20120929 |