CN205313639U - Extraction device - Google Patents
Extraction device Download PDFInfo
- Publication number
- CN205313639U CN205313639U CN201520938089.6U CN201520938089U CN205313639U CN 205313639 U CN205313639 U CN 205313639U CN 201520938089 U CN201520938089 U CN 201520938089U CN 205313639 U CN205313639 U CN 205313639U
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- China
- Prior art keywords
- filter
- import
- outlet
- valve
- extraction
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- 238000000605 extraction Methods 0.000 title claims abstract description 54
- 230000008676 import Effects 0.000 claims abstract description 44
- 238000002156 mixing Methods 0.000 claims abstract description 26
- 238000003756 stirring Methods 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 abstract description 9
- 230000007547 defect Effects 0.000 abstract description 4
- 238000009854 hydrometallurgy Methods 0.000 abstract description 2
- 230000009466 transformation Effects 0.000 abstract description 2
- 238000005352 clarification Methods 0.000 abstract 3
- 238000010924 continuous production Methods 0.000 abstract 1
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 239000008346 aqueous phase Substances 0.000 description 40
- 238000001556 precipitation Methods 0.000 description 10
- 239000012071 phase Substances 0.000 description 8
- 238000000926 separation method Methods 0.000 description 7
- 208000035126 Facies Diseases 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 229910052761 rare earth metal Inorganic materials 0.000 description 2
- 150000002910 rare earth metals Chemical class 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000012857 repacking Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
Classifications
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
The utility model provides an extraction device, belongs to resource cyclic utilization and hydrometallurgy equipment technical field. Including clarification chamber (1), stirring rake (2) and mixing chamber (3), stirring rake (2) are arranged in mixing chamber (3), its characterized in that know how things stand and feel confident (18) clarification chamber (1), import (13) in addition, filter (15) and export (17), the sealed end (18) or the lateral wall that is fixed in clarification chamber (1) of export (17), import (13) is sealed be fixed in export (17) on, import (13) certainly and extremely exports and have filter (15) through the pipe connection between (17). The third phase in the extraction tank also can be handled to the outstanding absurd creature material that is suitable for the extraction or turns over and come together and contain the insoluble matter. The specially adapted adopts the occasion industrialization continuous production who deposits anti - organic looks of coming together. Simple structure has, convenient to use, and throughput is big, easily produces the defect of insoluble matter jam extraction tanks such as third phase when having overcome the extraction turbid liquid. Can the transformation of the way of wear -out extraction tank.
Description
Technical field
This utility model relates to a kind of hydrometallurgy liquid liquid solvent extraction extraction equipment, belongs to hydrometallurgical plant technical field, is useful as extracting and back extraction equipment.
Background technology
Extraction tank is a kind of extraction equipment wet method, is the conventional separation equipment of metallurgical industry. Extraction tank is structurally generally identical with back extraction groove, but effect difference. Conventional extraction tank is suitable to extract the cleaning feed liquid without insoluble matter.
Notification number is CN2771220Y, the patent No. is 200520069968.6, name is called that the Chinese utility model patent of " unit rare-earth extracting tank " discloses a kind of unit rare-earth extracting tank, has extraction process normal, third phase thickness object cleaning cycle length and production efficiency high.
As extracted or when stripping process there is a large amount of insoluble matter (during especially with precipitation stripping method), the extraction tank of this patent disclosure will cannot be carried out operation because of insoluble matter Yu Sai clarifying chamber.
Utility model content
This utility model provides a kind of suspended material being suitable to and extracting or back extraction contains insoluble matter, it is possible to effectively overcome the defect that above prior art exists. It is particularly suitable for use with the occasion of precipitation back extraction organic facies.
Technical solutions of the utility model are as follows:
A kind of extraction equipment, including clarifying chamber 1, stirring paddle 2 and mixing chamber 3, described stirring paddle 2 is arranged in mixing chamber 3. Wherein said clarifying chamber 1 also has import 13, filter 15, outlet 17 and the end 18, described outlet 17 is sealingly fastened in the end 18 or the sidewall of clarifying chamber 1, described import 13 is sealingly fastened on outlet 17, is connected to filter 15 by pipeline from import 13 between outlet 17.
One of this utility model optimal technical scheme, also includes riser 5, and described riser 5 is that clarifying chamber 1 shares with mixing chamber 3.
The another optimal technical scheme of this utility model, also includes baffle plate 14, and described baffle plate 14 is positioned at and is fixed on clarifying chamber 1 lower sidewall, and baffle plate 14 keeps off in import 13, and baffle plate 14 has the opening 19 for material circulation.
The another optimal technical scheme of this utility model, the described end 18 is wedged bottom, and described outlet 17 is positioned at the minimum point at the end 18.
The another optimal technical scheme of this utility model, the described end 18 is the cone end.
The another optimal technical scheme of this utility model, also includes valve 12, and described valve 12, between import 13 and filter 15, is connected with import 13 and filter 15 respectively by pipeline.
The another optimal technical scheme of this utility model, also includes valve 11, and described valve 11 is connected by pipe-and-filter 15 after being positioned at filter 15.
The another optimal technical scheme of this utility model, also includes pump 16, and described pump 16, between filter 15 and outlet 17, is connected with filter 15, outlet 17 respectively by pipeline.
The another optimal technical scheme of this utility model, also includes valve 21 and outlet 22, and described outlet 22 is positioned in the middle part of clarifying chamber 1, is connected with valve 21, pump 16 respectively successively by pipeline.
The another optimal technical scheme of this utility model, also includes outlet 23 and valve 24, and described outlet 23 is positioned in the middle part of mixing chamber 3, is connected with valve 21, pump 16 successively by pipeline.
This utility model has the advantage that
1, not change remove clean by insoluble matter under the premise of extraction tank operating mode, it is to avoid insoluble matter Yu Sai clarifying chamber and destroy the defect of extraction tank operating mode;
2, make and easy to use, it is possible to existing old extraction tank repacking.
3, the third phase in mixing chamber, clarifying chamber can be extracted.
Accompanying drawing explanation
Accompanying drawing 1 is embodiment 3 schematic diagram.
Accompanying drawing 2 is embodiment 4 schematic diagram.
Accompanying drawing 3 is embodiment 1,2 schematic diagram.
Accompanying drawing 4 is embodiment 5,6 schematic diagram.
Detailed description of the invention
Embodiment 1
Referring to Fig. 3.
Precipitation back extraction groove, including clarifying chamber 1, stirring paddle 2 and mixing chamber 3, described stirring paddle 2 is arranged in mixing chamber 3. Wherein said clarifying chamber 1 has flat 18, also have import 13, filter 15, pump 16 and outlet 17, described outlet 17 is sealingly fastened in the bottom of clarifying chamber 1 sidewall, and described import 13 is sealingly fastened on outlet 17, is connected to filter 15 by pipeline from import 13 between outlet 17.
During use, precipitant stirs the insoluble matter reacting generation after mixing with organic facies agitated oar 2 in mixing chamber 3 and organic facies, aqueous phase together enter 1 point, clarifying chamber phase. Because organic facies density is little, floating on upper strata, aqueous phase densities is relatively big, is positioned at lower floor. The density of insoluble matter relatively aqueous phase is bigger, is settled down to gradually bottom clarifying chamber 1. Extracting under the current drive that aqueous phase produces at pump 16, insoluble matter is sent to filter 15 by pump 16 together with aqueous phase and separates. After separation, insoluble matter is stayed in filter 15, and aqueous phase returns to clarifying chamber 1.
Therefore, precipitate back extraction groove described in the present embodiment when keeping clarifying chamber's 1 original duty, insoluble matter removed from clarifying chamber 1, it is to avoid insoluble matter Yu Sai clarifying chamber and destroy the defect of back extraction groove operating mode.
The present embodiment can be reequiped with old extraction tank.
Embodiment 2
Referring to Fig. 3.
Extraction tank, including clarifying chamber 1, stirring paddle 2 and mixing chamber 3, described stirring paddle 2 is arranged in mixing chamber 3. Wherein said clarifying chamber 1 has flat 18, also have import 13, baffle plate 14, filter 15, pump 16 and outlet 17, described outlet 17 is sealingly fastened in the bottom of clarifying chamber 1 sidewall, described import 13 is sealingly fastened on outlet 17, is connected to filter 15 by pipeline from import 13 between outlet 17. Described baffle plate 14 is rectangular, flatly keeps off above import 13, and three limits are sealingly fastened in the bottom of clarifying chamber 1 wall, has for aqueous phase and opening 19 that also molten thing passes through between another limit and clarifying chamber 1 wall of baffle plate 14.
During work, insoluble matter is fallen below baffle plate 14 along opening 19, is sent to filter 15 by pump 16 together with aqueous phase and separates. After separation, insoluble matter is stayed in filter 15, and aqueous phase returns to clarifying chamber 1. Baffle plate 14 blocks the disturbance of the water opposing flaps upper liquid returning to clarifying chamber 1. Organic facies and aqueous phase above precipitation back extraction groove clarifying chamber 1 baffle plate 14 are not subject to return the impact of clarifying chamber 1 aqueous phase.
Embodiment 3
Referring to Fig. 1.
Extraction tank, including clarifying chamber 1, stirring paddle 2 and mixing chamber 3, described stirring paddle 2 is arranged in mixing chamber 3. Wherein said clarifying chamber 1 has wedged bottom 18, also have valve 11, valve 12, import 13, slanting baffle 14, filter 15, pump 16 and outlet 17, described outlet 17 is sealingly fastened in the minimum point bottom clarifying chamber 1, described import 13 is sealingly fastened under slanting baffle 14 peak, is connected with in turn filter 15 and valve 12 between import 13 to outlet 17 by pipeline. Described slanting baffle 14 is rectangular, and from import 13 block cover import 13 obliquely down over, three limits are sealingly fastened in the bottom of clarifying chamber 1 wall, has the opening 19 passed through for aqueous phase and insoluble matter between a limit and clarifying chamber 1 wall that slanting baffle 14 is minimum. Described valve 11 is connected by pipe-and-filter 15 after being positioned at filter 15.
During work, insoluble matter and the aqueous phase on part slanting baffle 14 enter below slanting baffle 14 along opening 19, are delivered to filter 15 with the aqueous phase below slanting baffle 14 by pump 16 and separate. After separation, insoluble matter stays periodic cleaning in filter 15; A part of aqueous phase controls to return the lower section of clarifying chamber 1 slanting baffle 14 through valve 12, and a part of aqueous phase controls to go next stage back extraction groove or otherwise processed through valve 11. It is in insoluble matter being in tilted layout essentially without being deposited on slanting baffle 14 because of slanting baffle 14 above whole clarifying chamber 1 slanting baffle 14. Slanting baffle 14 also blocks the aqueous phase returning to clarifying chamber 1 disturbance to slanting baffle upper liquid. Aqueous phase above precipitation back extraction groove clarifying chamber 1 slanting baffle 14 is not by the impact of the aqueous phase returning to clarifying chamber 1.
Embodiment 4
Referring to Fig. 2.
Precipitation back extraction groove, including clarifying chamber 1, stirring paddle 2 and mixing chamber 3, described stirring paddle 2 is arranged in mixing chamber 3. Wherein said clarifying chamber 1 has at the bottom of the stupefied cone of downward four 18, also have valve 11, valve 12, import 13, baffle plate 14, filter 15, pump 16 and outlet 17, described outlet 17 is sealingly fastened in the minimum point of 18 at the bottom of four stupefied cones, described import 13 is sealingly fastened under baffle plate 14 peak, is connected with in turn filter 15 and valve 12 between import 13 to outlet 17 by pipeline. Described baffle plate 14 is in four downward stupefied tapers, block cover import 13 above import 13; Four edges is all sealingly fastened in the bottom of clarifying chamber 1 wall, has the opening 19 passed through for aqueous phase and insoluble matter at the bottom of four stupefied cones of baffle plate 14. Described valve 11 is connected by pipe-and-filter 15 after being positioned at filter 15.
During work, insoluble matter and the aqueous phase on part baffle plate 14 enter below baffle plate 14 along opening 19, are sent to filter 15 with the aqueous phase below baffle plate 14 by pump 16 and separate. After separation, insoluble matter is stayed in filter 15; A part of aqueous phase controls to return the lower section of clarifying chamber 1 baffle plate 14 through valve 12, and a part of aqueous phase controls to go next stage back extraction groove or otherwise processed through valve 11. It is in the insoluble matter above whole clarifying chamber 1 baffle plate 14 because the tapered arrangement of baffle plate 14 is essentially without being deposited on baffle plate 14.Baffle plate 14 also blocks the disturbance of the water opposing flaps upper liquid returning to clarifying chamber 1. Aqueous phase above precipitation back extraction groove clarifying chamber 1 baffle plate 14 is not by the impact of the aqueous phase returning to clarifying chamber 1.
Embodiment 5
Referring to Fig. 4.
Precipitation back extraction groove, including clarifying chamber 1, stirring paddle 2 and mixing chamber 3, described stirring paddle 2 is arranged in mixing chamber 3. Wherein said clarifying chamber 1 has at the bottom of the stupefied cone of downward four 18, also have valve 21, valve 10, valve 11, valve 12, import 13, baffle plate 14, filter 15, pump 16, outlet 17 and outlet 22, described outlet 17 is sealingly fastened in the minimum point of 18 at the bottom of four stupefied cones, described import 13 is sealingly fastened under baffle plate 14 peak, is connected with in turn filter 15 and valve 12 between import 13 to outlet 17 by pipeline. Described baffle plate 14 is in four downward stupefied tapers, block cover import 13 above import 13; Four edges is all sealingly fastened in the bottom of clarifying chamber 1 wall, has the opening 19 passed through for aqueous phase and insoluble matter at the bottom of four stupefied cones of baffle plate 14. Described valve 11 is connected by pipe-and-filter 15 after being positioned at filter 15. Described outlet 22 is positioned in the middle part of clarifying chamber 1, by connecting with the import of pump 16 after pipeline connecting valve 21.
During work, insoluble matter and the aqueous phase on part baffle plate 14 enter below baffle plate 14 along opening 19, are sent to filter 15 with the aqueous phase below baffle plate 14 by pump 16 and separate. After separation, insoluble matter is stayed in filter 15; A part of aqueous phase controls to return the lower section of clarifying chamber 1 baffle plate 14 through valve 12, and a part of aqueous phase controls to go next stage back extraction groove or otherwise processed through valve 11. It is in the insoluble matter above whole clarifying chamber 1 baffle plate 14 because the tapered arrangement of baffle plate 14 is essentially without being deposited on baffle plate 14. Baffle plate 14 also blocks the disturbance of the water opposing flaps upper liquid returning to clarifying chamber 1. Aqueous phase above precipitation back extraction groove clarifying chamber 1 baffle plate 14 is not by the impact of the aqueous phase returning to clarifying chamber 1.
If desired, it is possible to by the third phase controlled in extraction clarifying chamber 1 of valve 10 and valve 21. The third phase extracted is deposited in filter 15.
Embodiment 6
Referring to Fig. 4.
Extraction tank, including clarifying chamber 1, stirring paddle 2 and mixing chamber 3, described stirring paddle 2 is arranged in mixing chamber 3. Wherein said clarifying chamber 1 has at the bottom of the stupefied cone of downward four 18, also has valve 21, valve 24, valve 10, valve 11, valve 12, import 13, baffle plate 14, filter 15, pump 16, outlet 17, outlet 22 and outlet 24. Described outlet 17 is sealingly fastened in the minimum point of 18 at the bottom of four stupefied cones, and described import 13 is sealingly fastened under baffle plate 14 peak, is connected with in turn filter 15 and valve 12 between import 13 to outlet 17 by pipeline. Described baffle plate 14 is in four downward stupefied tapers, block cover import 13 above import 13; Four edges is all sealingly fastened in the bottom of clarifying chamber 1 wall, has the opening 19 passed through for aqueous phase and insoluble matter at the bottom of four stupefied cones of baffle plate 14. Described valve 11 is connected by pipe-and-filter 15 after being positioned at filter 15. Described outlet 22 is positioned in the middle part of clarifying chamber 1, by connecting with the import of pump 16 after pipeline connecting valve 21.
During work, insoluble matter and the aqueous phase on part baffle plate 14 enter below baffle plate 14 along opening 19, are sent to filter 15 with the aqueous phase below baffle plate 14 by pump 16 and separate. After separation, insoluble matter is stayed in filter 15; A part of aqueous phase controls to return the lower section of clarifying chamber 1 baffle plate 14 through valve 12, and a part of aqueous phase controls to go next stage back extraction groove or otherwise processed through valve 11.It is in the insoluble matter above whole clarifying chamber 1 baffle plate 14 because the tapered arrangement of baffle plate 14 is essentially without being deposited on baffle plate 14. Baffle plate 14 also blocks the disturbance of the water opposing flaps upper liquid returning to clarifying chamber 1. Aqueous phase above precipitation back extraction groove clarifying chamber 1 baffle plate 14 is not by the impact of the aqueous phase returning to clarifying chamber 1.
If desired, it is possible to by the third phase controlled in outlet 22 extraction clarifying chamber 1 of valve 10 and valve 21; By valve 10 and valve 11, valve 12, valve 24 the third phases controlled in outlet 23 extraction mixing chambers 3. The third phase extracted is deposited in filter 15.
Finally it should be noted that, below it is only several optimal ways cited by this utility model, it will be understood by those skilled in the art that this utility model embodiment is not limited to above several, any equivalent transformation made on basis of the present utility model, all should belong to category of the present utility model.
Claims (10)
1. an extraction equipment, including clarifying chamber (1), stirring paddle (2) and mixing chamber (3), described stirring paddle (2) is arranged in mixing chamber (3), it is characterized in that there is the end (18) described clarifying chamber (1), also has import (13), filter (15) and outlet (17), described outlet (17) is sealingly fastened in the end (18) or the sidewall of clarifying chamber (1), described import (13) is sealingly fastened on outlet (17), between outlet (17), it is connected to filter (15) by pipeline from import (13).
2. extraction tank as claimed in claim 1, it is characterised in that also including riser (5), described riser (5) shares with mixing chamber (3) for clarifying chamber (1).
3. extraction tank as claimed in claim 1, characterized by further comprising baffle plate (14), described baffle plate (14) is positioned at and is fixed on clarifying chamber (1) lower sidewall, baffle plate (14) gear is in import (13) top, and baffle plate (14) has the opening (19) for material circulation.
4. extraction equipment as claimed in claim 1, it is characterised in that the described end (18) are wedged bottom, and described outlet (17) is positioned at the minimum point of the end (18).
5. extraction equipment as claimed in claim 4, it is characterised in that the described end (18) are the cone end.
6. extraction equipment as claimed in claim 1, characterized by further comprising valve (12), described valve (12) is positioned between import (13) and filter (15), is connected with import (13) and filter (15) respectively by pipeline.
7. extraction equipment as claimed in claim 6, it is characterised in that also include valve (11), described valve (11) is connected by pipe-and-filter (15) after being positioned at filter (15).
8. extraction equipment as claimed in claim 1, characterized by further comprising pump (16), described pump (16) is positioned between filter (15) and outlet (17), is connected with filter (15), outlet (17) successively by pipeline.
9. extraction equipment as claimed in claim 1, characterized by further comprising valve (21) and outlet (22), described outlet (22) is positioned at middle part, clarifying chamber (1), is connected with valve (21), pump (16) respectively successively by pipeline.
10. extraction equipment as described in as arbitrary in claim 1-9, characterized by further comprising outlet (23) and valve (24), described outlet 23 is positioned at mixing chamber (3) middle part, is connected with valve (21), pump (16) successively by pipeline.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420711286X | 2014-11-24 | ||
| CN201420711286 | 2014-11-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205313639U true CN205313639U (en) | 2016-06-15 |
Family
ID=56311937
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520938089.6U Active CN205313639U (en) | 2014-11-24 | 2015-11-23 | Extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205313639U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109321750A (en) * | 2018-10-10 | 2019-02-12 | 紫金矿业集团股份有限公司 | A method of processing extraction process generates three-phase |
-
2015
- 2015-11-23 CN CN201520938089.6U patent/CN205313639U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109321750A (en) * | 2018-10-10 | 2019-02-12 | 紫金矿业集团股份有限公司 | A method of processing extraction process generates three-phase |
| CN109321750B (en) * | 2018-10-10 | 2020-06-19 | 紫金矿业集团股份有限公司 | Method for treating three phases generated in extraction process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: An extraction device Effective date of registration: 20210107 Granted publication date: 20160615 Pledgee: Ganzhou Branch of Bank of Communications Co.,Ltd. Pledgor: GANZHOU RECYCLE NEW TECHNOLOGY Co.,Ltd. Registration number: Y2021980000161 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20231019 Granted publication date: 20160615 Pledgee: Ganzhou Branch of Bank of Communications Co.,Ltd. Pledgor: GANZHOU RECYCLE NEW TECHNOLOGY Co.,Ltd. Registration number: Y2021980000161 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |