CN207153273U - A kind of device for improving magnesium sulfate quality - Google Patents
A kind of device for improving magnesium sulfate quality Download PDFInfo
- Publication number
- CN207153273U CN207153273U CN201720999830.9U CN201720999830U CN207153273U CN 207153273 U CN207153273 U CN 207153273U CN 201720999830 U CN201720999830 U CN 201720999830U CN 207153273 U CN207153273 U CN 207153273U
- Authority
- CN
- China
- Prior art keywords
- magnesium sulfate
- concentration tower
- additionally provided
- separator
- pipeline
- 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
Links
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
The utility model discloses a kind of device for improving magnesium sulfate quality, including concentration tower, concentration tower is provided with suspension separating liquid refluxing opening, brilliant material mixture export is additionally provided with below suspension separating liquid refluxing opening, crystalline substance material mixture export is connected by the first pipeline with the import of levitated pump, the outlet of levitated pump is connected by second pipe with the first solidliquid mixture import of primary separator, the bottom of primary separator is additionally provided with the first underflow opening, and the first underflow opening is connected by the 3rd pipeline with magnesium sulfate crystallization apparatus.Magnesium sulfate crystals and dope can be expected to separate in mixed liquor by the utility model by primary separator eddy flow from crystalline substance, are reduced the impurity content of magnesium sulfate, improved the quality of magnesium sulfate finished product；Impurity inside clear liquid containing fine impurity particle is separated by feeding filter by second-stage separator, sends clear liquid back to concentration tower again, can effectively prevent concentration tower fouling and line clogging, and improve the utilization rate of raw material.
Description
Technical field
The utility model belongs to field of chemical equipment, is related to a kind of magnesium sulfate, specifically a kind of raising magnesium sulfate quality
Device.
Background technology
In current magnesium sulfate preparation process, its quality cannot be guaranteed always, and traditional raising magnesium sulfate quality
Device does not accomplish the impurity content of very effective reduction magnesium sulfate, improves the quality of magnesium sulfate finished product.And in lifting process
In easily there is concentration tower fouling, the situation that line clogging and part material waste occurs.To solve drawbacks described above, now provide a kind of
Solution.
Utility model content
The purpose of this utility model is to provide a kind of device for improving magnesium sulfate quality.
The purpose of this utility model can be achieved through the following technical solutions：
A kind of device for improving magnesium sulfate quality, including concentration tower, concentration tower are provided with suspension separating liquid refluxing opening, suspend
Brilliant material mixture export, crystalline substance material import of the mixture export by the first pipeline and levitated pump are additionally provided with below separating liquid refluxing opening
It is connected, the outlet of levitated pump is connected by second pipe with the first solidliquid mixture import of primary separator, a fraction
Bottom from device is additionally provided with the first underflow opening, and the first underflow opening is connected by the 3rd pipeline with magnesium sulfate crystallization apparatus；
Further, the first overfall is additionally provided with the primary separator, the first overfall passes through the first central tube
It is connected with the second solidliquid mixture import of second-stage separator.
Further, the second overfall is additionally provided with the second-stage separator, the second overfall passes through the second central tube
It is connected with the suspension separating liquid refluxing opening on concentration tower.
Further, the bottom of the second-stage separator is additionally provided with the second underflow opening, and the second underflow opening passes through the 4th pipeline
It is connected with filter.
Further, filter is plate and frame type filter-press.
The beneficial effects of the utility model：The utility model can be by magnesium sulfate crystals and dope by primary separator eddy flow
Expect to separate in mixed liquor from crystalline substance, reduce the impurity content of magnesium sulfate, improve the quality of magnesium sulfate finished product；Pass through the second-order separation
Impurity inside clear liquid containing fine impurity particle is separated feeding filter by device, and clear liquid is sent back to concentration again
Tower, concentration tower fouling and line clogging can be effectively prevented, and improve the utilization rate of raw material.
Brief description of the drawings
For the ease of it will be appreciated by those skilled in the art that being further described below in conjunction with the accompanying drawings to the utility model.
Fig. 1 is the utility model structure diagram.
Embodiment
As shown in figure 1, a kind of device for improving magnesium sulfate quality, including concentration tower 1, concentration tower 1 are provided with to suspend and separated
Liquid refluxing opening 101, the lower section of suspension separating liquid refluxing opening 101 are additionally provided with brilliant material mixture export 102；Crystalline substance material mixture export 102
It is connected by the first pipeline 201 with the import of levitated pump 2, the outlet of levitated pump 2 passes through second pipe 202 and primary separator
3 the first solidliquid mixture import 301 is connected, and the top of the first solidliquid mixture import 301 is provided with the first overfall 302；The
One overfall 302 is connected by the first central tube 304 with the second solidliquid mixture import 401 of second-stage separator 4, containing thin
The clear liquid of micro- impurity particle is discharged into second-stage separator 4 from the central tube at the top of primary separator 3.On second-stage separator 4
The second overfall 402 is additionally provided with, the second overfall 402 is flowed back by the second central tube 404 with the suspension separating liquid on concentration tower 1
Mouth 101 connects, and in the presence of centrifugal inertial force, clear liquid is back to concentration tower 1 from the top center pipe discharge of second-stage separator 4
It is interior, further concentration.
The bottom of primary separator 3 is additionally provided with the first underflow opening 303, and the first underflow opening 303 passes through the 3rd pipeline 305 and sulphur
Sour magnesium crystallization apparatus 6 connects, and the Adlerika after concentrating in concentration tower is sent into primary separator 3 by levitated pump 2, inertia from
In the presence of mental and physical efforts, substantial amounts of magnesium sulfate crystals and dope eddy flow are to the bottom of primary separator 3, the magnesium sulfate crystals that eddy flow gets off
And dope is sent into magnesium sulfate crystallization apparatus by pipeline 7 again；
The bottom of second-stage separator 4 is additionally provided with the second underflow opening 403, and the second underflow opening 403 passes through the 4th pipeline 405 and mistake
Filter device 5 connects, and filter 5 is plate and frame type filter-press, in the presence of centrifugal inertial force, contains fine impurity particle eddy flow
To the bottom of second-stage separator 4, fine impurity that eddy flow gets off is delivered to plate filter 5 by the 4th pipeline 405 and handled.
A kind of device for improving magnesium sulfate quality, it is at work, mixed from the brilliant material of the brilliant material mixture export outflow of concentration tower
Close liquid and primary separator is entered by levitated pump, magnesium sulfate crystals and dope eddy flow are expected by mixed liquor from crystalline substance by primary separator
In separate, and be sent to magnesium sulfate crystallization apparatus extraction.And the clear liquid containing fine impurity particle is from primary separator
The central tube at top is discharged into second-stage separator.In the presence of centrifugal inertial force, containing fine impurity particle eddy flow extremely
Second-stage separator bottom, the fine impurity that eddy flow gets off deliver to filter processing again；Clear liquid is from the top of second-stage separator
The discharge of heart pipe is back in concentration tower, further concentration.The utility model by primary separator eddy flow by magnesium sulfate crystals and
Dope expects to separate in mixed liquor from crystalline substance, reduces the impurity content of magnesium sulfate, improves the quality of magnesium sulfate finished product；Pass through two level
Impurity inside clear liquid containing fine impurity particle is separated feeding filter by separator, clear liquid is sent back to again dense
Contracting tower, concentration tower fouling and line clogging can be effectively prevented, and improve the utilization rate of raw material.
Above content is only to the utility model structure example and explanation, the technology people of affiliated the art
Member is made various modifications or supplement to described specific embodiment or substituted using similar mode, without departing from reality
With new structure or surmount scope defined in the claims, the scope of protection of the utility model all should be belonged to.
Claims (5)
1. a kind of device for improving magnesium sulfate quality, it is characterised in that including concentration tower (1), concentration tower (1), which is provided with to suspend, to be divided
Chaotropic refluxing opening (101), suspension separating liquid refluxing opening (101) lower section are additionally provided with brilliant material mixture export (102), crystalline substance material mixed liquor
Outlet (102) is connected by the first pipeline (201) with the import of levitated pump (2), and the outlet of levitated pump (2) passes through second pipe
(202) it is connected with the first solidliquid mixture import (301) of primary separator (3), the bottom of primary separator (3) is additionally provided with
First underflow opening (303), the first underflow opening (303) are connected by the 3rd pipeline (305) with magnesium sulfate crystallization apparatus (6).
A kind of 2. device for improving magnesium sulfate quality according to claim 1, it is characterised in that the primary separator
(3) the first overfall (302) is additionally provided with, the first overfall (302) passes through the first central tube (304) and second-stage separator
(4) the second solidliquid mixture import (401) is connected.
A kind of 3. device for improving magnesium sulfate quality according to claim 2, it is characterised in that the second-stage separator
(4) the second overfall (402) is additionally provided with, the second overfall (402) passes through on the second central tube (404) and concentration tower (1)
Suspension separating liquid refluxing opening (101) connection.
A kind of 4. device for improving magnesium sulfate quality according to claim 3, it is characterised in that the second-stage separator
(4) bottom is additionally provided with the second underflow opening (403), and the second underflow opening (403) passes through the 4th pipeline (405) and filter (5)
Connection.
A kind of 5. device for improving magnesium sulfate quality according to claim 4, it is characterised in that the filter (5)
For plate and frame type filter-press.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720999830.9U CN207153273U (en) | 2017-08-10 | 2017-08-10 | A kind of device for improving magnesium sulfate quality |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720999830.9U CN207153273U (en) | 2017-08-10 | 2017-08-10 | A kind of device for improving magnesium sulfate quality |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207153273U true CN207153273U (en) | 2018-03-30 |
Family
ID=61715878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720999830.9U Expired - Fee Related CN207153273U (en) | 2017-08-10 | 2017-08-10 | A kind of device for improving magnesium sulfate quality |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207153273U (en) |
-
2017
- 2017-08-10 CN CN201720999830.9U patent/CN207153273U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208098394U (en) | The combination centrifugal device of a small amount of fine particle impurity in a kind of separation liquid | |
| WO2021047266A1 (en) | Apparatus and method for increasing solid content in reaction crystallizer | |
| CN102011001B (en) | Feeding device and method for cadmium-removing boiling purification tank system | |
| CN207153273U (en) | A kind of device for improving magnesium sulfate quality | |
| CN208964572U (en) | A kind of solid kind medicine dissolving and adding all-in-one machine | |
| CN215427456U (en) | Hydrometallurgy leaches rich liquid clarifier | |
| CN211752836U (en) | Zirconium oxychloride crystal separation and suction filtration tank | |
| CN206549309U (en) | A kind of new take-off pond | |
| CN206063955U (en) | A kind of solid-liquid continuous separation device | |
| CN207545889U (en) | One kind isolates and purifies system | |
| CN206483183U (en) | A kind of extraction mechanism and extraction equipment | |
| CN208087706U (en) | A kind of dezincification device for cobalt intermediate | |
| CN206654916U (en) | A kind of thalline extraction equipment of microbial fermentation solution | |
| CN219129224U (en) | Seed separating device | |
| CN212974290U (en) | Novel flue gas desulfurization thickener device | |
| CN210905077U (en) | Continuous extraction device | |
| CN206483184U (en) | A kind of extraction mechanism and extraction element | |
| CN219128582U (en) | Solid-liquid separation device for salt-containing wastewater treatment | |
| CN216457420U (en) | Membrane separation device for high-concentration fruit and vegetable juice raw stock | |
| CN217535986U (en) | Virus particle antigen purification and concentration equipment | |
| CN208574269U (en) | A kind of high density suspension formula clarifier | |
| CN209596663U (en) | A kind of sewage treatment tower | |
| CN208318163U (en) | Konjaku flour purifying plant | |
| CN212356636U (en) | Extraction oil removing equipment | |
| CN210481471U (en) | Silver ion leaching system in manganese ore silver ion separation system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180330 Termination date: 20190810 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |