CN205046173U - Draw rare earth's automated production system in fly ash - Google Patents
Draw rare earth's automated production system in fly ash Download PDFInfo
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- CN205046173U CN205046173U CN201520750525.7U CN201520750525U CN205046173U CN 205046173 U CN205046173 U CN 205046173U CN 201520750525 U CN201520750525 U CN 201520750525U CN 205046173 U CN205046173 U CN 205046173U
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- rare earth
- production system
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- extraction
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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Abstract
The utility model discloses be applied to drawing of in fly ash rare earth, relate to a draw rare earth's automated production system in fly ash, including the pretreatment of raw material unit that connects gradually, middle processing unit and back processing unit, pretreatment of raw material unit, middle processing unit and back processing unit all with the system control unit connection. Compared with the prior art, the utility model discloses a hardware systems integrates the management, can realize the automated control of whole technology, and the personnel of need not carry out the operation of intermediate links such as corresponding detection, transport, has promoted the efficiency of processing, has also reduced workman's intensity of labour simultaneously.
Description
Technical field
The utility model is applied to the extraction of flyash rare earth elements, relates to the mechanized production system of Extraction of rare earth element in a kind of flyash.
Background technology
At present, to the removal process more complicated of flyash rare earth elements, although each equipment is all provided with analysis and detection device, if detect result does not have in claimed range after certain apparatus processing completes, then need to return in this equipment and again process, because technical process is more, between each operation, synergetic property is not strong, and material transfer needs manually to have come between each equipment, so require higher to concrete operations workman, cause working efficiency lower.
Utility model content
The technical problems to be solved in the utility model is: prior art gathers the removal process more complicated of flyash rare earth elements, higher to the requirement of operator, inefficiency, for solving the problem, provides a kind of removal process more complicated of flyash rare earth elements.
The purpose of this utility model realizes in the following manner:
The mechanized production system of Extraction of rare earth element in flyash, comprise the feed material preparation units, intermediate treatment unit and the post-processing unit that connect successively, feed material preparation units, intermediate treatment unit are all connected with system control unit with post-processing unit.
Feed material preparation units comprises magnetic separator, grading machine and flotation machine, magnetic separator, is provided with material conveyor belt between grading machine and the feed inlet and outlet of flotation machine; Intermediate treatment unit comprises the reactor and centrifugal extractor that are connected by pipeline, and reactor is connected by pipeline with the flotation machine of feed material preparation units; Post-processing unit is crystallizer, and crystallizer is connected by the centrifugal extractor of pipeline with intermediate treatment unit.
Material conveyer belt is driven by clockwise and anticlockwise motor, and clockwise and anticlockwise motor is connected with system control unit; Pipeline is provided with magnetic valve, and magnetic valve is connected with system control unit.
Magnetic separator, grading machine, flotation machine, reactor, centrifugal extractor and crystallizer are all provided with analysis and detection device, and analysis and detection device is all connected with system control unit.
System control unit is computer.
Relative to prior art, the utility model, by the integration Management of hardware system, can realize the Automated condtrol of whole technique, detect accordingly without the need to personnel, the operation of the middle-chain such as carrying, improve the efficiency of processing, also reduce the labour intensity of workman simultaneously.
Accompanying drawing explanation
Fig. 1 is the utility model system principle diagram.
Fig. 2 is the utility model operation system structure schematic diagram.
wherein, 1 is material conveyor belt; 2 is magnetic separators; 3 is analysis and detection devices; 4 is grading machines; 5 is flotation machine; 6 is reactors; 7 is centrifugal extractors; 8 is crystallizers; 9 is product storage devices.
Embodiment
As Figure 1-Figure 2, in flyash, the mechanized production system of Extraction of rare earth element, mainly comprises system control unit, feed material preparation units, intermediate treatment unit and post-processing unit, and wherein system control unit is computer; Feed material preparation units is integrated with corresponding pre-processing device: magnetic separator 2, grading machine 4 and flotation machine 5, and the feed inlet and outlet between each equipment is interconnected, and material realizes the transmission of material between links by material conveyor belt 1; Intermediate treatment unit is integrated with corresponding intermediate treatment facility: reactor 6 and centrifugal extractor 7, reactor 6 is connected with above-mentioned flotation machine 5 by corresponding pipeline, receive the flyash after previous step pre-treatment, reactor 6 is connected by pipeline with centrifugal extractor 7 simultaneously, is received in the material after reaction in reactor 6; Post-processing unit is integrated with corresponding finishing apparatus: crystallizer 8, and crystallizer 8 is connected with above-mentioned centrifugal extractor 7 by corresponding pipeline equally.
Except the connection between hardware device, central controller is also connected with the analysis and detection device 3 on each equipment, operating device runs, if if the material after its process of the powdered coal ash that processed by magnetic separator 2 is after corresponding analysis and detection device 3 detects, do not reach goal-selling, then computer controls travelling belt by controlling to drive the clockwise and anticlockwise motor of material conveyor belt, material is sent into again magnetic separator 2 and carries out secondary treatment, until meet preset requirement; If if the material after its process of the powdered coal ash of flotation machine 5 process is after corresponding analysis and detection device 3 detects, do not reach goal-selling, then computer is by controlling the magnetic valve on pipeline, by ducted material reflow to flotation machine 5, until meet preset requirement.The rare earth element of final extraction enters in product storage device 9.
By the integration Management of hardware system, the Automated condtrol of whole technique can be realized, detect accordingly without the need to personnel, the operation of the middle-chain such as carrying, improve the efficiency of processing, also reduce the labour intensity of workman simultaneously.
Claims (5)
1. the mechanized production system of Extraction of rare earth element in flyash, it is characterized in that: comprise the feed material preparation units, intermediate treatment unit and the post-processing unit that connect successively, feed material preparation units, intermediate treatment unit are all connected with system control unit with post-processing unit.
2. the mechanized production system of Extraction of rare earth element in flyash according to claim 1, it is characterized in that: feed material preparation units comprises magnetic separator, grading machine and flotation machine, magnetic separator, between grading machine and the feed inlet and outlet of flotation machine, be provided with material conveyor belt; Intermediate treatment unit comprises the reactor and centrifugal extractor that are connected by pipeline, and reactor is connected by pipeline with the flotation machine of feed material preparation units; Post-processing unit is crystallizer, and crystallizer is connected by the centrifugal extractor of pipeline with intermediate treatment unit.
3. the mechanized production system of Extraction of rare earth element in flyash according to claim 2, it is characterized in that: material conveyer belt is driven by clockwise and anticlockwise motor, clockwise and anticlockwise motor is connected with system control unit; Pipeline is provided with magnetic valve, and magnetic valve is connected with system control unit.
4. the mechanized production system of Extraction of rare earth element in flyash according to claim 2, it is characterized in that: magnetic separator, grading machine, flotation machine, reactor, centrifugal extractor and crystallizer are all provided with analysis and detection device, and analysis and detection device is all connected with system control unit.
5. the mechanized production system of Extraction of rare earth element in the flyash according to claim arbitrary in claim 1-4, is characterized in that: system control unit is computer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520750525.7U CN205046173U (en) | 2015-09-25 | 2015-09-25 | Draw rare earth's automated production system in fly ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520750525.7U CN205046173U (en) | 2015-09-25 | 2015-09-25 | Draw rare earth's automated production system in fly ash |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205046173U true CN205046173U (en) | 2016-02-24 |
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ID=55339771
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520750525.7U Expired - Fee Related CN205046173U (en) | 2015-09-25 | 2015-09-25 | Draw rare earth's automated production system in fly ash |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205046173U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106772030A (en) * | 2016-11-10 | 2017-05-31 | 中铝广西国盛稀土开发有限公司 | Rare-earth smelting separates intelligent motor monitoring system |
| CN110872106A (en) * | 2018-08-31 | 2020-03-10 | 贵州芭田生态工程有限公司 | Phosphorite preparation system with balanced processing speed in each link |
| CN117517040A (en) * | 2024-01-04 | 2024-02-06 | 煤炭科学技术研究院有限公司 | Analysis method of physical enrichment index of rare earth elements in fly ash and physical enrichment method of rare earth elements in fly ash |
-
2015
- 2015-09-25 CN CN201520750525.7U patent/CN205046173U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106772030A (en) * | 2016-11-10 | 2017-05-31 | 中铝广西国盛稀土开发有限公司 | Rare-earth smelting separates intelligent motor monitoring system |
| CN110872106A (en) * | 2018-08-31 | 2020-03-10 | 贵州芭田生态工程有限公司 | Phosphorite preparation system with balanced processing speed in each link |
| CN117517040A (en) * | 2024-01-04 | 2024-02-06 | 煤炭科学技术研究院有限公司 | Analysis method of physical enrichment index of rare earth elements in fly ash and physical enrichment method of rare earth elements in fly ash |
| CN117517040B (en) * | 2024-01-04 | 2024-03-08 | 煤炭科学技术研究院有限公司 | Analysis method of physical enrichment index of rare earth elements in fly ash and physical enrichment method of rare earth elements in fly ash |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160224 Termination date: 20160925 |