CN207628567U - Classify after waste lithium ion is broken retracting device - Google Patents
Classify after waste lithium ion is broken retracting device Download PDFInfo
- Publication number
- CN207628567U CN207628567U CN201721250986.3U CN201721250986U CN207628567U CN 207628567 U CN207628567 U CN 207628567U CN 201721250986 U CN201721250986 U CN 201721250986U CN 207628567 U CN207628567 U CN 207628567U
- Authority
- CN
- China
- Prior art keywords
- sieve plate
- separation chamber
- lithium ion
- air pressure
- broken
- 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.)
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- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium Ion Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 21
- 239000002699 waste material Substances 0.000 title claims abstract description 18
- 238000000926 separation method Methods 0.000 claims abstract description 53
- 239000011229 interlayer Substances 0.000 claims abstract description 17
- 238000005192 partition Methods 0.000 claims abstract description 8
- 239000010410 layer Substances 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 76
- 206010018987 Haemorrhage Diseases 0.000 claims description 19
- 230000000740 bleeding Effects 0.000 claims description 19
- 231100000319 bleeding Toxicity 0.000 claims description 19
- 239000010419 fine particle Substances 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 8
- 238000007664 blowing Methods 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 9
- 239000000126 substance Substances 0.000 abstract description 3
- 238000004065 wastewater treatment Methods 0.000 abstract description 3
- 238000011084 recovery Methods 0.000 abstract description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N lithium Chemical compound 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[Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 15
- 229910052744 lithium Inorganic materials 0.000 description 15
- 239000011889 copper foil Substances 0.000 description 12
- 239000005030 aluminium foil Substances 0.000 description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 11
- 239000002253 acid Substances 0.000 description 10
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt Chemical compound 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[Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 10
- 229910052803 cobalt Inorganic materials 0.000 description 10
- 239000010941 cobalt Substances 0.000 description 10
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- 230000000694 effects Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 208000001187 Dyskinesias Diseases 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound 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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/84—Recycling of batteries or fuel cells
Abstract
The utility model is related to waste lithium ion it is broken after classify retracting device, separation chamber's slant setting, it is arranged on bearing, high-end setting feed inlet, bottom end connect air pressure and take out diaphragm apparatus, and separation chamber is equipped with vibrating device, it is internally provided with sieve plate, the quantity of sieve plate is at least one, and inside separation chamber, the interlayer that sieve plate separates is separately connected discharge port；Air pressure takes out diaphragm apparatus and is equipped with partition board with top layer's sieve plate lower part.The effective combination for realizing pneumatic separating and screening sorting, simplifies equipment complexity, realizes simple and effective sorting.It makes full use of lithium ion battery different component to be crushed nature difference, realizes the classification recovery processing of size fractionated component.Belong to physical separation method, be not related to chemicals, wastewater treatment and secondary pollution problem is not present.The utility model pneumatic separating combines with screening, is integrated, process is easy, efficient.
Description
Technical field
The utility model is related to retracting device field of classifying, especially a kind of pneumatic separating and screening combination, integrated, mistake
Classify after easy, the efficient waste lithium ion of journey is broken retracting device.
Background technology
Pneumatic separating method effectively overcomes floating product dehydration as dry separation mode with screening separating method and gives up
Water treatment problems are widely used in the sortings such as coal, mineral field, technology relative maturity, but in electron wastes
The especially discarded lithium battery process field in field is using less.
In discarded lithium battery shattering process, since lithium battery respectively forms some mechanical mechanical property difference, metal shell
It plays a protective role to battery, therefore there is higher mechanical strength, there is larger granularity after being crushed；Diaphragm has stronger
Toughness is difficult that its is fine crushing in shattering process, so diaphragm also has larger granularity；Copper foil is relatively thin thin with aluminium foil
Piece is easy to form bulk bead of the size less than shell with diaphragm in shattering process；Cobalt acid lithium is viscous by PVDF with graphite
Knot itself is exactly tiny particle on aluminium foil is with copper foil, is mixed with graphite so obtaining thinner cobalt acid lithium after broken
Powder.
In the prior art, a kind of pneumatic separating is needed to be combined with screening, is integrated, process is easy, efficient discarded lithium
Classify after ion battery is broken retracting device.
Utility model content
The purpose of this utility model is to provide a kind of pneumatic separating and is combined with screening, is integrated, is process simplicity, efficient
Classify after waste lithium ion is broken retracting device.
Classify after waste lithium ion is broken retracting device, including：
Separation chamber, separation chamber's slant setting are arranged on bearing, high-end setting feed inlet, and bottom end connects air pressure and takes out
Diaphragm apparatus, the separation chamber are equipped with vibrating device, are internally provided with sieve plate, the quantity of the sieve plate be it is at least one, it is described
Inside separation chamber, the interlayer that sieve plate separates is separately connected discharge port；
The air pressure takes out diaphragm apparatus and is equipped with partition board with top layer's sieve plate lower part.
The sieve plate is equipped with rotating brushes.
It is negative suction system or blowing device that diaphragm apparatus is taken out in the air pressure.
It includes air guiding chamber, wind turbine, deduster and air pressure bleeding point that diaphragm apparatus is taken out in the air pressure, and the air pressure bleeding point is set
It sets on the top of separation chamber, the air guiding chamber is arranged in the lower part of separation chamber, and extraction diaphragm is collected in the air pressure bleeding point connection
Deduster, the deduster connects wind turbine.
The deduster is fixed on deduster holder.
There are two the sieve plate is set, it is followed successively by macroporous plate and aperture sieve plate, the macroporous plate, small hole sizer from top to bottom
Separation chamber is divided into three interlayers, the interlayer and particulate of the aperture sieve plate and bottom plate composition by the bottom plate of plate and separation chamber bottom
The interlayer of grade material discharge port conducting, the macroporous plate and aperture sieve plate composition is connected with middle grade material discharge port, described
Macroporous plate is connected with the interlayer that the top of separation chamber forms with big grade material discharge port.
Fine particle stage material material collecting tank, the middle grade material discharge port lower section are set below the fine particle stage material discharge port
Big grade material material collecting tank is arranged in grade material material collecting tank in setting, the big grade material discharge port lower section.
The air pressure bleeding point is arranged in the top of macroporous plate, the big grade material discharge port opening direction and sorting
The longitudinal direction of room is identical, and close to air pressure bleeding point, and rotating brushes is equipped between the macroporous plate and aperture sieve plate.
Elastic bearing is equipped between the bearing and separation chamber.
The elastic bearing is flexible two sections connecting rod.
The utility model separation chamber slant setting, be arranged on bearing, high-end setting feed inlet, bottom end connect air pressure take out every
Film device, separation chamber are equipped with vibrating device, are internally provided with sieve plate, and the quantity of sieve plate is at least one, inside separation chamber, sieve plate
The interlayer separated is separately connected discharge port；Air pressure takes out diaphragm apparatus and is equipped with partition board with top layer's sieve plate lower part.Realize wind-force point
Effective combination of choosing and screening sorting, simplifies equipment complexity, realizes simple and effective sorting.Make full use of lithium ion battery not
It is crushed nature difference with component, realizes the classification recovery processing of size fractionated component.Belong to physical separation method, is not related to chemical drugs
Wastewater treatment and secondary pollution problem is not present in product.The utility model pneumatic separating combines with screening, is integrated, process is simple
Just, efficient.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model；
In figure：1, separation chamber, 2, feed inlet, 3, macroporous plate, 4, aperture sieve plate, 5, bottom plate, 6, elastic bearing, 7, branch
Seat, 8, fine particle stage material discharge port, 9, fine particle stage material material collecting tank, 10, middle grade material material collecting tank, 11, middle grade material goes out
Material mouth, 12, air guiding chamber, 13, big grade material material collecting tank, 14, big grade material discharge port, 15, deduster holder, 16, wind turbine,
17, deduster, 18, air pressure bleeding point, 19, partition board, 20, rotating brushes, 21, vibrating device.
Specific implementation mode
Below in conjunction with the drawings and specific embodiments, the utility model is described further.
Embodiment 1：
Classify after waste lithium ion is broken retracting device, including：Separation chamber 1,1 slant setting of separation chamber, setting exist
On bearing 7, high-end setting feed inlet 2, bottom end connects air pressure and takes out diaphragm apparatus, and separation chamber 1 is equipped with vibrating device 21, and inside is set
There is sieve plate, the quantity of sieve plate is at least one, and inside separation chamber 1, the interlayer that sieve plate separates is separately connected discharge port；Air pressure take out every
Film device is equipped with partition board 19 with top layer's sieve plate lower part.
Sieve plate is equipped with rotating brushes 20.It is negative suction system or blowing device that diaphragm apparatus is taken out in air pressure.Air pressure is taken out
Diaphragm apparatus includes air guiding chamber 12, wind turbine 16, deduster 17 and air pressure bleeding point 18, and air pressure bleeding point 18 is arranged in separation chamber 1
Top, air guiding chamber 12 is arranged in the lower part of separation chamber 1, and the deduster 17 of extraction diaphragm is collected in the connection of air pressure bleeding point 18, is removed
Dirt device 17 connects wind turbine 16.Deduster 17 is fixed on deduster holder 15.
There are two sieve plate is set, it is followed successively by macroporous plate 3 and aperture sieve plate 4, macroporous plate 3,4 and of aperture sieve plate from top to bottom
Separation chamber 1 is divided into three interlayers, the interlayer and fine fraction object that aperture sieve plate 4 and bottom plate 5 form by the bottom plate 5 of 1 bottom of separation chamber
Expect that discharge port 8 is connected, the interlayer that macroporous plate 3 and aperture sieve plate 4 form is connected with middle grade material discharge port 11, macroporous plate
3 interlayer and the conducting of big grade material discharge port 14 with the top composition of separation chamber 1.The 8 lower section setting of fine particle stage material discharge port
Fine particle stage material material collecting tank 9, grade material material collecting tank 10 in the 11 lower section setting of middle grade material discharge port, big grade material discharging
Big grade material material collecting tank 13 is arranged in 14 lower section of mouth.Air pressure bleeding point 18 is arranged in the top of macroporous plate 3, and big grade material goes out
14 opening direction of material mouth is identical as the longitudinal direction of separation chamber 1, and close to air pressure bleeding point 18, between macroporous plate 3 and aperture sieve plate 4
Equipped with rotating brushes 20.
Elastic bearing 6 is equipped between bearing 7 and separation chamber 1.Elastic bearing 6 is flexible two sections connecting rod.
Broken lithium ion battery mixed material is fed by feed inlet 2 and is fallen in macroporous plate 3, is acted in mechanical oscillation
The materials such as lower granularity smaller copper foil, aluminium foil, cobalt acid lithium and graphite drop into the smaller aperture sieve plate 4 of sieve pore, and granularity is minimum
Cobalt acid lithium the bottom plate 5 of 1 bottom of separation chamber is directly fallen on by aperture sieve plate 4 with graphite, while aperture sieve plate 4 is fitted with rotation
The graphite on copper foil and aluminium foil can will be attached to under cobalt acid lithium brush by turning hairbrush 20.Not by sieve pore material in mechanical vibration force
And continues forward slip under gravity and be finally classified collection.Diaphragm on macroporous plate 3 is then under gas pressure
Deduster 17 is sucked, sorting purpose is reached.Big grade plastics and shell, middle grade aluminium are finally respectively obtained in different material collecting tanks
Foil, with graphite, is convenient for follow-up separation with copper foil, small grade cobalt acid lithium.
The utility model includes separation chamber 1, feed inlet 2, macroporous plate 3, aperture sieve plate 4, bottom plate 5, elastic bearing 6, branch
Seat 7, fine particle stage material discharge port 8, fine particle stage material material collecting tank 9, middle grade material material collecting tank 10, middle grade material discharge port
11, air guiding chamber 12, big grade material material collecting tank 13, big grade material discharge port 14, deduster holder 15, wind turbine 16, deduster
17, air pressure bleeding point 18, partition board 19, rotating brushes 20, vibrating device 21.Separation chamber 1 is fixed on bearing 7 by elastic bearing 6
Above, mechanical vibration force is provided by vibrating device 21, makes material along inclined screen panel vibration, reaches screening purpose；In griddle
It is provided with rotating brushes 20 between plate 3 and aperture sieve plate 4, it is carried out clearly when copper foil is moved with aluminium foil on aperture sieve plate
It sweeps, so that the cobalt acid lithium for being attached to surface is fallen off with graphite and fall on the bottom plate of separation chamber through aperture sieve plate.Bulky grain shell with every
When film runs to air pressure suction opening 18, provides air pressure by wind turbine 16 and cause air flow through air guiding chamber 12 into separation chamber 1, diaphragm is by band
It walks to be collected into deduster 17, other big grade materials then fall into big grade material material collecting tank 13 and are collected.Different grains
The material of grade, along inclined-plane slide downward, falls into corresponding material collection finally by respective discharge port and fills under shock effect
It sets, completes sorting and material collection.
Separation chamber 1 is by feed inlet 2, macroporous plate 3, aperture sieve plate 4, bottom plate 5, elastic bearing 6, bearing 7, fine fraction object
Expect that discharge port 8, middle grade material discharge port 11, big grade material discharge port 14 form, by adjusting the vibration frequency of vibrating device 21
Rate can control the oscillation intensity of separation chamber 1.It is provided with inclined partition board 19 between air guiding chamber 12 and middle grade discharge port 11, can be prevented
Only copper foil, aluminium foil dyskinesias under the action of the wind.Rotating brushes 20 is arranged between macroporous plate 3 and aperture sieve plate 4, turns
Speed is adjustable, realizes to being attached to cleaning of the copper foil with graphite on aluminium foil with cobalt acid lithium.17 one end of deduster and air pressure bleeding point 18
It is connected, the other end is connected with wind turbine 16, and according to material actual conditions, adjusting wind-force is big by frequency converter adjusts rotation speed of fan
It is small.
Separation chamber 1 is equipped with feed inlet 2, macroporous plate 3, aperture sieve plate 4, bottom plate 5, fine particle stage material discharge port 8, middle grain
Grade material discharge port 11, big grade material discharge port 14 are filled with the separation chamber that fixing bracket is connected in vibration by elastic bearing
It sets and is in vibration condition under 21 effects, the broken mixed material of lithium battery is fed by feed inlet 2 in separation chamber, greatly
Grade shell and diaphragm become griddle oversize and are moved down under mechanical oscillation effect, the diaphragm quilt at air pressure bleeding point 18
It siphons away and is collected into deduster；Copper foil aluminium foil then becomes small hole sizer oversize, in the rotating brushes along sieve plate down motion process
20 pairs of copper foil aluminium foils clean, and the graphite being attached to above copper foil aluminium foil falls off with cobalt acid lithium；Cobalt acid lithium is then fallen with graphite
To above bottom plate 5, final each grade material is collected by discharge port into corresponding material collecting tank.
The utility model has the following advantages compared with prior art：
(1) the effective combination for realizing pneumatic separating and screening sorting, simplifies equipment complexity, realizes simple and effective point
Choosing.
(2) it makes full use of lithium ion battery different component to be crushed nature difference, realizes the classification recycling of size fractionated component
Processing.
(3) the utility model belongs to physical separation method, is not related to chemicals, and wastewater treatment and secondary pollution is not present
Problem.
The utility model pneumatic separating is the same as screening sorting is combined, integration sorts, assorting room simplicity, the efficiency of separation
Rotating brushes high, on sieve plate remains attached to after being crushed under the electrode material brush on copper foil and aluminium foil.
The basic principles and main features and advantage of the utility model have been shown and described above.The technical staff of the industry
It should be appreciated that the present utility model is not limited to the above embodiments, the above embodiments and description only describe this
The principle of utility model, on the premise of not departing from the spirit and scope of the utility model the utility model also have various change and
It improves, these various changes and improvements fall within the scope of the claimed invention.The utility model requires protection scope by
Appended claims and its equivalent define.
Claims (10)
- Retracting device of classifying after 1. waste lithium ion is broken, which is characterized in that including：Separation chamber, separation chamber's slant setting are arranged on bearing, high-end setting feed inlet, and bottom end connects air pressure and takes out diaphragm Device, the separation chamber are equipped with vibrating device, are internally provided with sieve plate, the quantity of the sieve plate is at least one, the sorting Chamber interior, the interlayer that sieve plate separates are separately connected discharge port；The air pressure takes out diaphragm apparatus and is equipped with partition board with top layer's sieve plate lower part.
- Retracting device of classifying after 2. waste lithium ion according to claim 1 is broken, which is characterized in that the sieve plate It is equipped with rotating brushes.
- Retracting device of classifying after 3. waste lithium ion according to claim 1 or 2 is broken, which is characterized in that described It is negative suction system or blowing device that diaphragm apparatus is taken out in air pressure.
- Retracting device of classifying after 4. waste lithium ion according to claim 1 or 2 is broken, which is characterized in that described It includes air guiding chamber, wind turbine, deduster and air pressure bleeding point that diaphragm apparatus is taken out in air pressure, and the air pressure bleeding point is arranged in separation chamber Top, the air guiding chamber are arranged in the lower part of separation chamber, and the deduster of extraction diaphragm is collected in the air pressure bleeding point connection, described Deduster connects wind turbine.
- Retracting device of classifying after 5. waste lithium ion according to claim 4 is broken, which is characterized in that the dedusting Device is fixed on deduster holder.
- Retracting device of classifying after 6. waste lithium ion according to claim 1 or 2 is broken, which is characterized in that described There are two sieve plate is set, it is followed successively by macroporous plate and aperture sieve plate, the macroporous plate, aperture sieve plate and separation chamber bottom from top to bottom Separation chamber is divided into three interlayers, the interlayer and fine particle stage material discharge port of the aperture sieve plate and bottom plate composition by the bottom plate in portion Conducting, the macroporous plate and aperture sieve plate composition interlayer be connected with middle grade material discharge port, the macroporous plate and divide The interlayer that the top of room forms is selected to be connected with big grade material discharge port.
- Retracting device of classifying after 7. waste lithium ion according to claim 6 is broken, which is characterized in that the particulate Fine particle stage material material collecting tank, grade material collection in being arranged below the middle grade material discharge port are set below grade material discharge port Big grade material material collecting tank is arranged in hopper, the big grade material discharge port lower section.
- Retracting device of classifying after 8. waste lithium ion according to claim 6 is broken, which is characterized in that the macropore Air pressure bleeding point is arranged in the top of sieve plate, and the big grade material discharge port opening direction is identical as the longitudinal direction of separation chamber, and leans on Nearly air pressure bleeding point.
- Retracting device of classifying after 9. waste lithium ion according to claim 1 or 2 is broken, which is characterized in that described Elastic bearing is equipped between bearing and separation chamber.
- Retracting device of classifying after 10. waste lithium ion according to claim 9 is broken, which is characterized in that the bullet Property bearing be it is flexible two save connecting rod.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721250986.3U CN207628567U (en) | 2017-09-27 | 2017-09-27 | Classify after waste lithium ion is broken retracting device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721250986.3U CN207628567U (en) | 2017-09-27 | 2017-09-27 | Classify after waste lithium ion is broken retracting device |
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| Publication Number | Publication Date |
|---|---|
| CN207628567U true CN207628567U (en) | 2018-07-20 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109174293A (en) * | 2018-09-20 | 2019-01-11 | 王志强 | A kind of waste power lithium battery core material electromagnetism combined sorting equipment |
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2017
- 2017-09-27 CN CN201721250986.3U patent/CN207628567U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109174293A (en) * | 2018-09-20 | 2019-01-11 | 王志强 | A kind of waste power lithium battery core material electromagnetism combined sorting equipment |
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