CN207805114U - A kind of microwave spiral leaching device - Google Patents
A kind of microwave spiral leaching device Download PDFInfo
- Publication number
- CN207805114U CN207805114U CN201820060772.8U CN201820060772U CN207805114U CN 207805114 U CN207805114 U CN 207805114U CN 201820060772 U CN201820060772 U CN 201820060772U CN 207805114 U CN207805114 U CN 207805114U
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- Prior art keywords
- reaction chamber
- reaction
- baffle
- chamber
- microwave
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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 is related to a kind of microwave spiral leaching devices, belong to microwave metallurgical technical field.Helical blade in the apparatus is fixed on agitating device, agitating device is in reaction chamber, the upper end of reaction chamber is equipped with feed inlet and the infrared temperature probe for thermometric, after material enters reaction chamber by feed inlet, reaction mass reacts required heat source and comes from magnetron in the reactor chamber, incubation cavity is in the outside of reaction chamber, for keeping reaction temperature and heat, baffle is equipped with below reaction chamber, one end of baffle is fixed on reaction chamber, the other end can move, aggregate bin and movable sieve are equipped with below baffle, pass through aggregate bin and portable screen Wondertek to the effect of separation of solid and liquid after material reacts fully in the reactor chamber, discharge port is used for collecting the leached mud and leachate after the completion of reaction, leached mud or leachate are obtained according to the difference of requirement of experiment.The device can effectively improve the leaching rate in metallurgical process, achieve the purpose that improve mineral utilization rate.
Description
Technical field
The utility model is related to a kind of microwave spiral leaching devices, belong to microwave metallurgical technical field.
Background technology
During non-ferrous metallurgy, resource recycling is an important production link, does not require nothing more than material
Efficiently separate, and require save production cost.Leaching process is a significant process during resource reclaim, therefore in smelting
It realizes that sufficient Leach reaction obtains higher leaching rate and becomes critically important during gold, and there is stirring not in leaching process
Uniformly, heating is uneven, causes to leach mineral conglomeration, leaches phenomena such as uneven.The utility model develops a kind of microwave spiral shell
Rotation leaching device can meet this requirement.The utility model, using microwave heating ore materials, reaches section on the basis of existing
Can, the purpose of emission reduction, achieve the purpose that mix well material, thermal energy and strengthen to react using auger.According to different leachings
Go out the stirring of condition setting difference and heating parameters to achieve the effect that leaching.Meanwhile the advantage by combining microwave heating, more
Soon, more completely, more thoroughly leaching material is enable preferably to complete leaching process.
Invention content
Technical problems to be solved]
The purpose of this utility model is to provide a kind of microwave spiral leaching device.
Technical solution]
In view of the problems of the existing technology and insufficient, the utility model provides a kind of microwave spiral leaching device, this reality
It is achieved through the following technical solutions with novel.
A kind of microwave spiral leaching device, the microwave spiral leaching device include magnetron 1, incubation cavity 2, reaction chamber
3, feed inlet 4, agitating device 5, infrared temperature probe 6, helical blade 7, baffle 8, aggregate bin 9, movable sieve 10, discharge port
11, helical blade 7 is fixed on agitating device 5, and agitating device 5 is placed in reaction chamber 3, and the upper end of reaction chamber 3 is equipped with feed inlet 4
With the infrared temperature probe 6 for thermometric, after material enters reaction chamber 3 by feed inlet 4, reaction mass is anti-in reaction chamber 3
Required heat source is answered to come from magnetron 1, incubation cavity 2 is in the outside of reaction chamber 3, for keeping reaction temperature and heat, anti-
3 lower section of chamber is answered to be equipped with baffle 8, one end of baffle 8 is fixed on reaction chamber 3, and the other end can move, and be set below baffle 8
There are aggregate bin 9 and movable sieve 10, is reached by aggregate bin 9 and movable sieve 10 after material reacts fully in reaction chamber 3
The effect of separation of solid and liquid, discharge port 11 is used for collecting the leached mud and leachate after the completion of reaction, according to the difference of requirement of experiment
Obtain leached mud or leachate.
A kind of microwave spiral leaching device, which is characterized in that the material composition of the helical blade 7 is poly- four
Vinyl fluoride has stronger toughness.
A kind of microwave spiral leaching device, which is characterized in that the movable sieve 10 can be according to different leachings
The particle size of material is selected.
The utility model has the beneficial effects that：The utility model is solved leaches uneven, leaching rate in metallurgical process
Not high feature, the purpose that the utility model combination microwave heating and auger are strengthened achieve the purpose that improve leaching rate；
Meanwhile by improving leaching rate, the cost consumption in metallurgical process is reduced, to improve the utilization rate of mineral.
【Description of the drawings】
Fig. 1 is the structural schematic diagram of the utility model.
In figure：1- magnetrons, 2- incubation cavities, 3- reaction chambers, 4- feed inlets, 5- agitating devices, 6- infrared temperature probes, 7-
Helical blade, 8- baffles, 9- aggregate bins, 10- activity sieves, 11- discharge ports.
【Specific implementation mode】
With reference to the accompanying drawings and detailed description, the utility model is described in further detail.
Embodiment 1
A kind of microwave spiral leaching device, which is characterized in that the microwave spiral leaching device includes magnetron 1, protects
Warm chamber 2, reaction chamber 3, feed inlet 4, agitating device 5, infrared temperature probe 6, helical blade 7, baffle 8, aggregate bin 9, portable screen
Net 10, discharge port 11, helical blade 7 are fixed on agitating device 5, and agitating device 5 is placed in reaction chamber 3, the upper end of reaction chamber 3
Infrared temperature probe 6 equipped with feed inlet 4 and for thermometric, after material enters reaction chamber 3 by feed inlet 4, reaction mass exists
Required heat source is reacted in reaction chamber 3 and comes from magnetron 1, and incubation cavity 2 is in the outside of reaction chamber 3, for keeping reaction temperature
And heat, baffle 8 is equipped with below reaction chamber 3, one end of baffle 8 is fixed on reaction chamber 3, and the other end can move, and keep off
It is equipped with aggregate bin 9 and movable sieve 10 below plate 8, passes through aggregate bin 9 and activity after material reacts fully in reaction chamber 3
Sieve 10 achievees the effect that separation of solid and liquid, and discharge port 11 is used for collecting the leached mud and leachate after the completion of reaction, according to experiment
It is required that difference obtain leached mud or leachate.
The material composition of the helical blade 7 of the device is polytetrafluoroethylene (PTFE), there is stronger toughness.
The movable sieve 10 of the device can be selected according to the different particle sizes for leaching material.
Above in association with attached drawing, the specific embodiments of the present invention are described in detail, but the utility model is not
It is limited to the above embodiment, within the knowledge of a person skilled in the art, this practicality can also be not being departed from
It is made a variety of changes under the premise of novel objective.
Claims (3)
1. a kind of microwave spiral leaching device, which is characterized in that the microwave spiral leaching device includes magnetron（1）, protect
Warm chamber（2）, reaction chamber（3）, feed inlet（4）, agitating device（5）, infrared temperature probe（6）, helical blade（7）, baffle（8）、
Aggregate bin（9）, movable sieve（10）, discharge port（11）, helical blade（7）It is fixed on agitating device（5）On, agitating device（5）
It is placed in reaction chamber（3）In, reaction chamber（3）Upper end be equipped with feed inlet（4）With the infrared temperature probe for thermometric（6）, material
Pass through feed inlet（4）Into reaction chamber（3）Afterwards, reaction mass is in reaction chamber（3）The middle required heat source of reaction comes from magnetron
（1）, incubation cavity（2）In reaction chamber（3）Outside, for keeping reaction temperature and heat, in reaction chamber（3）Lower section is equipped with baffle
（8）, baffle（8）One end be fixed on reaction chamber（3）On, the other end can move, in baffle（8）Below be equipped with aggregate bin
（9）With movable sieve（10）, when material is in reaction chamber（3）Pass through aggregate bin after middle reaction fully（9）With movable sieve（10）It reaches
To the effect of separation of solid and liquid, discharge port（11）For collecting leached mud and leachate after the completion of reaction, according to requirement of experiment
Difference obtains leached mud or leachate.
2. a kind of microwave spiral leaching device according to claim 1, which is characterized in that the helical blade（7）'s
Material composition is polytetrafluoroethylene (PTFE), there is stronger toughness.
3. a kind of microwave spiral leaching device according to claim 1, which is characterized in that the movable sieve（10）It can
It is selected according to the different particle sizes for leaching material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820060772.8U CN207805114U (en) | 2018-01-15 | 2018-01-15 | A kind of microwave spiral leaching device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820060772.8U CN207805114U (en) | 2018-01-15 | 2018-01-15 | A kind of microwave spiral leaching device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207805114U true CN207805114U (en) | 2018-09-04 |
Family
ID=63327220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820060772.8U Expired - Fee Related CN207805114U (en) | 2018-01-15 | 2018-01-15 | A kind of microwave spiral leaching device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207805114U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112831664A (en) * | 2021-03-22 | 2021-05-25 | 云南民族大学 | Manufacturing method of microwave-enhanced leaching device for leaching precious metals by using ionic liquid |
-
2018
- 2018-01-15 CN CN201820060772.8U patent/CN207805114U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112831664A (en) * | 2021-03-22 | 2021-05-25 | 云南民族大学 | Manufacturing method of microwave-enhanced leaching device for leaching precious metals by using ionic liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20180904 Termination date: 20190115 |