CN202954078U - Treatment system for separating tin-based metal materials from waste electrical appliances and electronic elements - Google Patents
Treatment system for separating tin-based metal materials from waste electrical appliances and electronic elements Download PDFInfo
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- CN202954078U CN202954078U CN2012206730555U CN201220673055U CN202954078U CN 202954078 U CN202954078 U CN 202954078U CN 2012206730555 U CN2012206730555 U CN 2012206730555U CN 201220673055 U CN201220673055 U CN 201220673055U CN 202954078 U CN202954078 U CN 202954078U
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- oil
- treatment system
- oil tank
- tank
- waste
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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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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a treatment system for separating tin-based metal materials from waste electrical appliances and electronic elements. The treatment system comprises a centrifuge, an oil tank and a heating machine, wherein an oil inlet at the upper end of the oil tank is connected with an oil outlet of the heating machine through a first oil pipe; an oil outlet at the lower end of the oil tank is connected with the oil inlet of the heating machine through a second oil pipe; heat conduction oil enters the heating machine through the second oil pipe, is heated by the heating machine and then is conveyed back into the oil tank through the first oil pipe; the centrifuge comprises a housing and a centrifugal cylinder mounted in the housing; and the centrifugal cylinder loading waste raw materials are placed in the oil tank, after the heat conduction oil is heated for melting tin, the centrifugal cylinder is further placed in the centrifuge, and the molten tin is separated and rotated to the inner wall of the housing from the waste raw materials by centrifugation so as to realize separation. The treatment system disclosed by the utility model can effectively recover the tin in the waste raw materials, shorten process flow, reduce energy consumption and reduce the emission of waste gas and waste liquid.
Description
Technical field
The utility model relates to the salvage material system, be specifically related to a kind of from the waste electrical equipment electronic component treatment system of Separation of Tin Base Metal material.
Background technology
Tin, fusing point is 232 ℃, is a kind of very important strategic material, especially concerning non-product tinnily, recycling tin is seemed to very important.Along with the development in epoch, people more and more pay attention to the idea of environment protection and Sustainable development.In January, 2006, European Union proposed environmental requirement to electron trade, carried out electronic product unleaded comprehensively, and the electronic welding material of China is used unleaded gun-metal to replace traditional tinsel material in succession.Gun-metal is with the obvious advantage on cost performance, and welding effect is good is vast electronic product machining exporter's first-selection processing materials.
A large amount of tinbase metallic substance that contain have been produced in hyundai electronics processing industry process of manufacture.The main employing by wet method electrolysis or fire reduction smelted and reclaimed the tinbase metallic substance both at home and abroad at present, demand strict technology, and complex process, the quality that reclaims product is uneven, and the rate of recovery is low, also can produce a large amount of dust and waste gas, the serious harm ecotope.
Therefore, for reclaiming the tinbase metallic substance, need to be improved existing method, be provided novel treatment system, efficient recovery tinbase metallic substance.
The utility model content
The purpose of this utility model is to provide a kind for the treatment of system, can effectively from waste and scrap, reclaim the tinbase metallic substance, and reduce energy consumption, shortened process.
Of the present utility model from waste and old raw material the treatment system of Separation of Tin Base Metal material, comprise whizzer, oil tank and heater; Wherein,
The upper end of described oil tank sets into hydraulic fluid port, and described oiler is connected with the oil outlet of described heater by the first oil pipe; The lower end of described oil tank sets out hydraulic fluid port, and described oil outlet is connected with the oiler of described heater by the second oil pipe; Thermal oil in described oil tank enters described heater through described the second oil pipe, through described heater heating, by described the first oil pipe, is transmitted back in described oil tank;
Described whizzer comprises: casing and the concentrator bowl be arranged in casing;
The concentrator bowl that described waste and old raw material is housed is placed in described oil tank, through heat-conducting oil heating, by after tin fusing, described concentrator bowl is placed in described whizzer, through centrifugal by the tin of fusing from waste and old raw material separating rotary to described casing inner wall.
In another preference, the bottom of described oil tank is provided with drain tap.
In another preference, described whizzer also comprises oil discharge outlet, through the centrifugal thermal oil screwed out from waste and old raw material, through described oil discharge outlet, discharges.
In another preference, the temperature of the thermal oil in described oil tank is 243-248 ℃.
In another preference, described oil tank comprises:
Tank body, described oiler is arranged on the upper end of described tank body, and described oil outlet is arranged on the lower end of described tank body;
Cover, described cover is removably mounted on the top of described tank body;
Thermal insulation layer, described thermal insulation layer is arranged on the periphery of described tank body.
In another preference, the thickness of described thermal insulation layer is 80-150mm.
In another preference, the bottom of described tank body is dished end, and described drain tap is arranged on the bottom of described dished end.
In another preference, described treatment system also comprises hanging apparatus, and described hanging apparatus for lifting described concentrator bowl between described whizzer and described oil tank.
In another preference in, described treatment system also comprises condensate recycling device, described condensate recycling device comprises:
Aerofoil fan, described aerofoil fan covers on the top of described oil tank;
Drainer, the top of described drainer arranges venting port, and bottom arranges oil discharge outlet, and lower end joins by condensation tracheae and described aerofoil fan;
Oil storage vessel, described oil storage vessel is arranged on the below of described drainer;
The mixed gas volatilized in described oil tank is sent into described condensing air pipework condensation through described aerofoil fan and is entered described drainer again, and the oil of condensation is discharged and entered described oil storage vessel through described oil discharge outlet, and gas is discharged through described venting port.
In another preference, described whizzer horizontal positioned.
Treatment system of the present utility model, not only can efficient recovery tin, with respect to existing technology, reduces energy consumption, and shortened process, reduce the discharge of waste gas and waste liquid, and thermal oil can recycle, reduces the pollution to environment.
In should be understood that in the utility model scope, above-mentioned each technical characterictic of the present utility model and can combining mutually between specifically described each technical characterictic in below (eg embodiment), thus form new or preferred technical scheme.As space is limited, tire out and state no longer one by one at this.
The accompanying drawing explanation
The structural representation that Fig. 1 is treatment system of the present utility model.
Embodiment
Below in conjunction with specific embodiment, further set forth the utility model.Should be understood that these embodiment only are not used in restriction scope of the present utility model for the utility model is described.The experimental technique of unreceipted actual conditions in the following example, usually according to normal condition or the condition of advising according to manufacturer.
As shown in Figure 1, of the present utility model from waste and old raw material the treatment system of Separation of Tin Base Metal material, comprise whizzer 1, oil tank 2 and heater 3; Wherein,
The upper end of described oil tank 2 sets into hydraulic fluid port 4, and described oiler 4 is connected with the oil outlet 6 of described heater 3 by the first oil pipe 5; The lower end of described oil tank 2 sets out hydraulic fluid port 7, and described oil outlet 7 is connected with the oiler 9 of described heater 3 by the second oil pipe 8; Thermal oil in described oil tank 2 enters described heater 3 through described the second oil pipe 8, through described heater 3 heating, by described the first oil pipe 5, is transmitted back in described oil tank 2;
Described whizzer 1 comprises: casing 10 and the concentrator bowl 11 be arranged in casing 10;
The concentrator bowl 11 that described waste and old raw material is housed is placed in described oil tank 2, after heat-conducting oil heating melts tin, described concentrator bowl 11 is placed in the casing 10 of described whizzer 1, through centrifugal, the tin of fusing is under centrifugal action, separate from waste and old raw material, throw away concentrator bowl 11, stick to described casing 10 inwalls.
Through heater 3 heating, make the temperature of the thermal oil in oil tank 2 maintain 243-248 ℃, make the tin fusing in waste and old raw material.
Described whizzer 1 also comprises oil discharge outlet 12, through the centrifugal thermal oil screwed out from waste and old raw material, through described oil discharge outlet 12, discharges.
The bottom of described oil tank 2 is provided with drain tap 13, for discharging the thermal oil in oil tank 2.
In a preference, described oil tank 2 comprises:
Tank body 14, described oiler 4 is arranged on the upper end of described tank body 14, and described oil outlet 7 is arranged on the lower end of described tank body 14;
Cover 15, described cover 15 is removably mounted on the top of described tank body 14;
The thermal insulation layer (not shown), described thermal insulation layer is arranged on the periphery of described tank body 14.
In a preference, the thickness of described thermal insulation layer is 80-150mm.
In a preference, the bottom of described tank body 14 is dished end 16, and described drain tap 13 is arranged on the bottom of described dished end 16.
In another preference, described treatment system also comprises the hanging apparatus (not shown), and described hanging apparatus for lifting described concentrator bowl between described whizzer and described oil tank.
In another preference, described treatment system also comprises condensate recycling device, and described condensate recycling device comprises:
Aerofoil fan 17, described aerofoil fan 17 covers on the top of described oil tank 2;
Drainer 18, the top of described drainer 18 arranges venting port 19, and bottom arranges oil discharge outlet 20, and lower end joins by condensation tracheae 21 and described aerofoil fan 17;
Oil storage vessel 22, described oil storage vessel 22 is arranged on the below of described drainer 18;
The mixed gas volatilized in described oil tank 2 is sent into described condensation tracheae 21 condensations through described aerofoil fan 17 and is entered described drainer 18 again, and the oil of condensation is discharged and entered described oil storage vessel 22 through described oil discharge outlet 20, and gas is discharged through described venting port 19.
In another preference, described whizzer 1 horizontal positioned.
While using treatment system of the present utility model, the concentrator bowl 11 that waste and old raw material is housed is inserted in oil tank 2.In oil tank 2, thermal oil is housed, thermal oil enters heater 3 through the second oil pipe 8, through heater 3 heating, by the first oil pipe 5, is transmitted back in oil tank 2.Thermal oil circulates between oil tank 2 and heater 3, makes the temperature of thermal oil maintain 243-248 ℃, makes the tin fusing in waste and old raw material.In this process, open condensate recycling device, will suck aerofoil fan 17 by the mixed gas of oil tank 1 volatilization, enter again drainer 18 in 21 condensations of condensation tracheae, the oil that condensation obtains is discharged and is entered oil storage vessel 22 through oil discharge outlet 20, and a small amount of gas is discharged through venting port 19, meets environmental requirement.
After the tin fusing, concentrator bowl 11 is inserted in whizzer 1 casing 10, through centrifugal, the tin of fusing and thermal oil are under centrifugal action, separate with waste and old raw material, throw away concentrator bowl 11, the tin of fusing sticks to casing 10 inwalls, thermal oil is discharged from oil discharge outlet 12, thus Separation and Recovery tinbase metallic substance.
Treatment system of the present utility model, comply with the requirement of resource recycling, overcome the conventional wet electrolysis, fire reduction is smelted the deficiency that prior art exists, utilize whizzer by waste and old raw material as isolated tin in electronic component, effectively reduce energy consumption, shortened process, reduce waste gas, the discharge of waste liquid, environmental contamination reduction.And can rapid heating, improve efficiency, safety automation.
Unless otherwise defined, the same meaning that all specialties of using in literary composition and scientific words and one skilled in the art are familiar.In addition, any method similar or impartial to described content and material all can be applicable in the utility model method.The use that better implementation method described in literary composition and material only present a demonstration.
All documents of mentioning at the utility model are all quoted as a reference in this application, just as each piece of document quoted separately as a reference.Should be understood that in addition those skilled in the art can make various changes or modifications the utility model after having read above-mentioned teachings of the present utility model, these equivalent form of values fall within the application's appended claims limited range equally.
Claims (10)
1. the treatment system of a Separation of Tin Base Metal material from waste and old raw material, is characterized in that, described treatment system comprises whizzer, oil tank and heater; Wherein,
The upper end of described oil tank sets into hydraulic fluid port, and described oiler is connected with the oil outlet of described heater by the first oil pipe; The lower end of described oil tank sets out hydraulic fluid port, and described oil outlet is connected with the oiler of described heater by the second oil pipe; Thermal oil in described oil tank enters described heater through described the second oil pipe, through described heater heating, by described the first oil pipe, is transmitted back in described oil tank;
Described whizzer comprises: casing and the concentrator bowl be arranged in casing;
The concentrator bowl that described waste and old raw material is housed is placed in described oil tank, through heat-conducting oil heating, by after tin fusing, described concentrator bowl is placed in described whizzer, through centrifugal by the tin of fusing from waste and old raw material separating rotary to described casing inner wall.
2. treatment system as claimed in claim 1, is characterized in that, the bottom of described oil tank is provided with drain tap.
3. treatment system as claimed in claim 1, is characterized in that, described whizzer also comprises oil discharge outlet, through the centrifugal thermal oil screwed out from waste and old raw material, through described oil discharge outlet, discharges.
4. treatment system as claimed in claim 1, is characterized in that, the temperature of the thermal oil in described oil tank is 243-248 ℃.
5. treatment system as claimed in claim 1, is characterized in that, described oil tank comprises:
Tank body, described oiler is arranged on the upper end of described tank body, and described oil outlet is arranged on the lower end of described tank body;
Cover, described cover is removably mounted on the top of described tank body;
Thermal insulation layer, described thermal insulation layer is arranged on the periphery of described tank body.
6. treatment system as claimed in claim 5, is characterized in that, the thickness of described thermal insulation layer is 80-150mm.
7. treatment system as claimed in claim 5, is characterized in that, the bottom of described tank body is dished end, and described drain tap is arranged on the bottom of described dished end.
8. treatment system as claimed in claim 1, is characterized in that, described treatment system also comprises hanging apparatus, and described hanging apparatus for lifting described concentrator bowl between described whizzer and described oil tank.
9. treatment system as claimed in claim 1, is characterized in that, described treatment system also comprises condensate recycling device, and described condensate recycling device comprises:
Aerofoil fan, described aerofoil fan covers on the top of described oil tank;
Drainer, the top of described drainer arranges venting port, and bottom arranges oil discharge outlet, and lower end joins by condensation tracheae and described aerofoil fan;
Oil storage vessel, described oil storage vessel is arranged on the below of described drainer;
The mixed gas volatilized in described oil tank is sent into described condensing air pipework condensation through described aerofoil fan and is entered described drainer again, and the oil of condensation is discharged and entered described oil storage vessel through described oil discharge outlet, and gas is discharged through described venting port.
10. treatment system as claimed in claim 1, is characterized in that, described whizzer horizontal positioned.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206730555U CN202954078U (en) | 2012-12-04 | 2012-12-04 | Treatment system for separating tin-based metal materials from waste electrical appliances and electronic elements |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206730555U CN202954078U (en) | 2012-12-04 | 2012-12-04 | Treatment system for separating tin-based metal materials from waste electrical appliances and electronic elements |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202954078U true CN202954078U (en) | 2013-05-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012206730555U Expired - Fee Related CN202954078U (en) | 2012-12-04 | 2012-12-04 | Treatment system for separating tin-based metal materials from waste electrical appliances and electronic elements |
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| CN (1) | CN202954078U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107739848A (en) * | 2017-10-19 | 2018-02-27 | 山西恒天镁业有限公司 | The Application way of magnesium condensation heat during a kind of production of magnesium by pidgeonprocess |
| CN113500051A (en) * | 2021-07-16 | 2021-10-15 | 兰州有色冶金设计研究院有限公司 | Circuit board soldering tin removing device and method |
-
2012
- 2012-12-04 CN CN2012206730555U patent/CN202954078U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107739848A (en) * | 2017-10-19 | 2018-02-27 | 山西恒天镁业有限公司 | The Application way of magnesium condensation heat during a kind of production of magnesium by pidgeonprocess |
| CN113500051A (en) * | 2021-07-16 | 2021-10-15 | 兰州有色冶金设计研究院有限公司 | Circuit board soldering tin removing device and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170407 Address after: 315400 Zhejiang city of Ningbo province Wolong new villa village of Yuyao City Li Zhou Street No. 53-1 Patentee after: Ningbo Island New Materials Co. Address before: 315400 Zhejiang city of Ningbo province Wolong new villa village of Yuyao City Li Zhou Street No. 53-1 Patentee before: Ningbo Shengzhidao Solder Material Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180930 Address after: 523601 Yao Shan Industrial Zone, Xie Gang Town, Dongguan, Guangdong (Dongguan Fei te Metal Technology Co., Ltd.) Patentee after: Dongguan Fei te Metal Technology Co., Ltd. Address before: 315400 Wolong 53-1, new Shu Village, Li Zhou street, Yuyao, Ningbo, Zhejiang Patentee before: Ningbo Island New Materials Co. |
|
| 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: 20130529 Termination date: 20191204 |