CN109256600B - Pollution-free lithium battery decomposition treatment system - Google Patents

Pollution-free lithium battery decomposition treatment system Download PDF

Info

Publication number
CN109256600B
CN109256600B CN201811321379.0A CN201811321379A CN109256600B CN 109256600 B CN109256600 B CN 109256600B CN 201811321379 A CN201811321379 A CN 201811321379A CN 109256600 B CN109256600 B CN 109256600B
Authority
CN
China
Prior art keywords
collector
iii
conveyed
airflow
spray tower
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.)
Active
Application number
CN201811321379.0A
Other languages
Chinese (zh)
Other versions
CN109256600A (en
Inventor
蔡保宪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gongyi Jixin Machinery Co ltd
Original Assignee
Gongyi Jixin Machinery Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Gongyi Jixin Machinery Co ltd filed Critical Gongyi Jixin Machinery Co ltd
Priority to CN201811321379.0A priority Critical patent/CN109256600B/en
Publication of CN109256600A publication Critical patent/CN109256600A/en
Application granted granted Critical
Publication of CN109256600B publication Critical patent/CN109256600B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/54Reclaiming serviceable parts of waste accumulators
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/84Recycling of batteries or fuel cells

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The application relates to the field of lithium battery treatment, in particular to a pollution-free lithium battery decomposition treatment system, which comprises a shredder, a crusher, an airflow separator, a magnetic separation conveyor, a crusher, an analyzer, a swinging sieve, a grinding machine and a rotary vibration sieve which are sequentially connected, wherein the shredder and the crusher are connected to a pulse dust collector I through pipelines, the airflow separator is connected with a collector I through a draught fan II, the collector I is connected to the pulse dust collector I, the pulse dust collector I is connected with a first air purification device through a high-pressure draught fan I, the analyzer is connected to a second air purification device through a collector II, the pulse dust collector II and the high-pressure draught fan II which are sequentially connected, the swinging sieve is connected with a collector III, the grinding machine is connected with a collector IV, the collector III and the collector IV are all connected to the pulse dust collector III, the pulse dust collector III is connected to the second air purification device through the high-pressure draught fan III, and the environment pollution is small, the energy utilization rate is high, and the recovery proportion is high.

Description

Pollution-free lithium battery decomposition treatment system
Technical Field
The application relates to the field of lithium battery treatment, in particular to a pollution-free lithium battery decomposition treatment system.
Background
Lithium batteries are one of the most commonly used batteries of electronic products at the present stage, and are mainly divided into lithium metal batteries and lithium ion batteries, wherein the lithium metal batteries generally use manganese dioxide as a positive electrode material, lithium metal or alloy metal thereof as a negative electrode material and use nonaqueous electrolyte solution; in general, lithium ion batteries are batteries using lithium alloy metal oxide as a positive electrode material, graphite as a negative electrode material, and nonaqueous electrolyte, and since the amount of lithium batteries is large and the update speed is high, a large amount of waste lithium batteries are generated, and the waste lithium batteries are decomposed and recycled into a concern.
The existing lithium battery decomposition treatment system mainly comprises a shredder, a crusher, an airflow separator, a magnetic separation conveyor, a crusher and an analyzer, and can decompose and recycle lithium batteries, but environmental pollution can be generated in the treatment process, and meanwhile, energy waste is caused.
Disclosure of Invention
The application aims to overcome the defects in the prior art and provide a pollution-free lithium battery decomposition treatment system with small environmental pollution, high energy utilization rate and high recovery ratio.
The application is realized by the following technical scheme: the utility model provides a pollution-free lithium cell decomposition processing system, includes shredder, breaker, air current sorter, magnetic separation conveyer, rubbing crusher, analysis machine, rocking screen, mill, the sieve that shakes soon that connects gradually, shredder and breaker all are connected to pulse dust remover I through the pipe connection, the air current sorter is connected with collector I through induced draft fan II, collector I is connected to pulse dust remover I, pulse dust remover I is connected with first air purification device through high-pressure induced draft fan I, the analysis machine is connected to second air purification device through collector II, pulse dust remover II, the high-pressure induced draft fan II that connect gradually, rocking screen is connected with collector III, the mill is connected with collector IV, collector III and collector IV all are connected to pulse dust remover III, pulse dust remover III is connected to second air purification device through high-pressure induced draft fan III.
Further, the first air purification device comprises a spray tower I connected with a high-pressure induced draft fan I, the spray tower I is connected with a UV photolysis air purifier I through a dryer I, and the UV photolysis air purifier I is connected with the induced draft fan I.
Further, the second air purification device comprises a spray tower II which is connected with a high-pressure induced draft fan II and a high-pressure induced draft fan II, wherein the spray tower II is connected with a UV photolysis air purifier II through a dryer I, and the UV photolysis air purifier II is connected with an induced draft fan III.
Further, the shredder includes frame I and the casing I that is located frame I, I upper end of casing is provided with feed inlet I, I both sides of frame are provided with drive arrangement I respectively, I interior both sides of casing are provided with the pivot I and the pivot II of being connected with drive arrangement I respectively, equal circumference distributes in pivot I and the pivot II has the blade, is equipped with the spacer between the adjacent blade, and the crisscross setting of blade in pivot I and the pivot II, I's lower extreme of casing is provided with discharge gate II.
Further, the crusher comprises a frame II, a shell II and a driving device II, wherein the shell II is positioned on the frame II, a feed inlet II is formed in one side of the upper end of the shell II, a crushing mechanism is arranged in the shell II and comprises a rotating shaft III, a fixed rod and a hammer head, the rotating shaft III is connected with the driving device II through a belt, the fixed rods are uniformly distributed on the circumference of the rotating shaft III and comprise n baffle plates perpendicular to the axis of the rotating shaft III and connecting rods penetrating through the end parts of the baffle plates, and the hammer head is sleeved on the connecting rods; the lower extreme of crushing mechanism is provided with the filter screen, the lower extreme of casing II is provided with the export.
Further, the hammer head is located on the connecting rod between the adjacent partition boards, a limiting block matched with the width of the hammer head is arranged on the connecting rod, and the distance from the connecting rod to the rotating shaft III is larger than the length of the hammer head.
Further, cyclone dust collectors are selected for the collector I, the collector II, the collector III and the collector IV.
Further, the crushing granularity of the crusher is 20-30 meshes.
Further, the grinding particle size of the grinder is 80-100 meshes.
The application has the beneficial effects that: the first air purifying device and the second air purifying device are arranged to purify the discharged air and prevent harmful gases from entering the ambient air; dust and macromolecular gas can be absorbed through the spray tower, and micromolecular harmful gas can be decomposed through the UV photolysis air purifier, so that air pollution is further reduced.
Drawings
FIG. 1 is a schematic illustration of an embodiment connection relationship;
FIG. 2 is a schematic front view of the shredder;
FIG. 3 is a schematic top view of the shredder;
FIG. 4 is a schematic side view of the shredder;
FIG. 5 is a schematic front view of a crusher;
FIG. 6 is a schematic side view of a crusher;
wherein: 1-frame I, 2-casing I, 3-feed inlet I, 4-pivot I, 5-pivot II, 6-motor, 7-speed reducer, 8-blade, 9-spacer, 10-discharge gate II, 11-frame II, 12-casing II, 13-feed inlet II, 14-pivot III, 15-tup, 16-baffle, 17-connecting rod, 18-stopper, 19-filter screen, 20-export.
Detailed Description
In the description of the present application, it should also be noted that, unless explicitly specified and limited otherwise, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present application will be understood in specific cases by those of ordinary skill in the art.
The following description of the embodiments of the present application will be made clearly and fully with reference to the accompanying drawings, in which it is evident that the embodiments described are only some, but not all embodiments of the application. All other embodiments, which can be made by those skilled in the art based on the embodiments of the application without making any inventive effort, are intended to be within the scope of the application.
Example 1
As shown in figures 1-6, a pollution-free lithium battery decomposition treatment system comprises a shredder, a crusher, an airflow separator, a magnetic separation conveyor, a crusher, an analysis machine, a swing sieve, a grinding machine and a rotary vibration sieve which are sequentially connected, wherein the upper ends of the shredder and the crusher are connected to a pulse dust remover I through pipelines, the airflow separator is connected with a collector I through a draught fan II, the collector I is connected to the pulse dust remover I, the pulse dust remover I is connected with a first air purification device through a high-pressure draught fan I, the analysis machine is connected to a second air purification device through a collector II, a pulse dust remover II and a high-pressure draught fan II which are sequentially connected, the swing sieve is connected with a collector III, the grinding machine is connected with a collector IV, the collector III and the collector IV are all connected to the pulse dust remover III, and the pulse dust remover III is connected to the second air purification device through the high-pressure draught fan III.
In the embodiment, the first air purifying device comprises a spray tower I connected with a high-pressure induced draft fan I, wherein the spray tower I is connected with a UV photolysis air purifier I through a dryer I, and the UV photolysis air purifier I is connected with the induced draft fan I;
the second air purification device comprises a spray tower II which is connected with a high-pressure induced draft fan II and a high-pressure induced draft fan II, the spray tower II is connected with a UV photolysis air purifier II through a dryer I, and the UV photolysis air purifier II is connected with an induced draft fan III.
In this embodiment, the shredder includes frame I1 and is located the casing I2 on frame I1, and feed inlet I3 is installed to casing I2 upper end, and in the feed inlet I3 got into casing I2 was followed to the material, drive arrangement I was installed respectively to frame I1 both sides, and pivot I4 and pivot II 5 that are connected with drive arrangement I are installed respectively to both sides in the casing I2, and pivot I4 and pivot II 5 centrosymmetric set up, and drive arrangement I includes motor 6 and speed reducer 7 that are connected through the belt. Blade 8 is evenly distributed on circumference in pivot I4 and pivot II 5, install spacer 9 between the adjacent blade 8, spacer 9 can fix a position blade 8, prevent that blade 8 from rocking about/removing, blade 8 crisscross setting in pivot I4 and the pivot II 5 makes blade 8 in pivot I4 correspond with spacer 9 positions in the pivot II 5, makes blade 8 in pivot I4 and the pivot II 5 crisscross each other, is located the lower extreme of casing I1 and is provided with discharge gate II 10, the material after shredding passes through the discharge gate II 10 ejection of compact.
The crusher comprises a frame II 11, a shell II 12 and a driving device II, wherein the shell II 12 and the driving device II are arranged on the frame II 11, a feed inlet II 13 is arranged on one side of the upper end of the shell II 12, materials enter the shell II 12 of the crusher through the feed inlet II 13, a crushing mechanism is arranged in the shell II 12 and comprises a rotating shaft III 14, a fixed rod and a hammer 15, the rotating shaft III 14 is connected with the driving device II through a belt, the fixed rod is uniformly distributed on the circumference of the rotating shaft III 14 and comprises n partition plates 16 perpendicular to the axis of the rotating shaft III 14 and a connecting rod 17 penetrating through the end parts of the partition plates 16, the hammer 15 is sleeved on the connecting rod 17, the hammer 15 is positioned on the connecting rod 17 between the adjacent partition plates 16, a limiting block 18 matched with the width of the hammer 15 is arranged on the connecting rod 17, the hammer 15 is prevented from moving left and right, the distance between the connecting rod 17 and the rotating shaft III is larger than the length of the hammer 15, the hammer 15 can rotate circumferentially along the connecting rod 17, the hammer 15 is driven to beat the materials under the rotation of the rotating shaft III 14, the rotating shaft III, the hammer impact and tear the materials to cause the materials to be crushed under the high-speed rotation of the hammer, the impact and the materials are provided with the fixed rods, the lower ends of the crushing mechanism are provided with 19, the materials, the size of the materials is separated from the materials through the filter screen 19 and the filter screen 12 and the size of the filter screen 20 is separated from the shell through the large size of the filter screen 12, and the size of the filter screen 20, and the material is discharged from the material through the filter screen 20.
In the embodiment, cyclone dust collectors are selected for the collector I, the collector II, the collector III and the collector IV.
In the decomposition treatment system for the pollution-free lithium battery provided by the embodiment, when a mobile phone plate-shaped battery is decomposed, the steel shell lithium battery is taken as an example, in the steel shell lithium battery, the steel shell is taken as the outer shell, the positive plate is taken as the aluminum foil, the negative plate is taken as the copper foil, the positive electrode material is lithium cobaltate, the negative electrode material is graphite, the diaphragm is a high polymer film, the electrolyte is ethylene carbonate dissolved with lithium hexafluorophosphate, the battery is put into a shredder and is broken down by the shredder, the diaphragm is broken down in the breaking process, the shredder and the shredder are operated, generated dust is conveyed to a pulse dust remover I through pipelines respectively arranged in the shredder and the shredder for primary filtration, then is conveyed to a spray tower I through a high-pressure induced draft fan I for secondary filtration, small-molecule harmful gas is still present in the air flow after filtration, and is subjected to tertiary filtration through a UV photolysis air purifier I, finally, and completely harmless gas is discharged outwards through the induced draft fan I, in the process, graphite powder with particle size of 0.05-0.1mm generated in the breaking and tearing down is discharged by the carbon dioxide through the air purifier I, and the carbon dioxide can be decomposed into water and environmental pollution by the spray tower I through the air purifier;
the crushed batteries are conveyed to an airflow separator through a conveying belt, dust and scattered diaphragms are conveyed to a collector I through a draught fan II under the action of airflow and vibration, dust in the collector 1 is conveyed to a pulse dust collector I for primary filtration, then is conveyed to a spray tower II through a high-pressure draught fan I for secondary filtration, micromolecular harmful gas is still present in the filtered airflow, the filtered airflow is subjected to tertiary filtration through a UV photolysis air purifier I, finally, completely harmless gas is obtained and is discharged outwards through the draught fan I, graphite powder with the particle size of 0.05-0.1mm, which is separated and escaped by the airflow, is absorbed by the spray tower I, and volatilized ethylene carbonate enters the UV photolysis air purifier I through a dryer for decomposition into carbon dioxide and water vapor for removal, so that the environmental pollution can be effectively reduced;
the method comprises the steps that materials which are not scattered in a battery in a crusher also enter a magnetic separation conveyor, crushed steel shells are separated, the separated materials enter the crusher to be crushed into 20-30 meshes, the crushed materials are conveyed to an analyzer, the upper end of the analyzer is connected with a pipeline, airflow of the analyzer is conveyed to a collector II through the pipeline, dust in the collector II is conveyed to a pulse dust collector II to be subjected to primary filtration, and then conveyed to a spray tower II through a high-pressure induced draft fan II to be subjected to secondary filtration, micromolecular harmful gases are also contained in the filtered airflow, the filtered harmful gases are subjected to tertiary filtration through a UV photolysis air purifier II, finally, completely harmless gases are obtained, and are discharged outwards through a draft fan III, and graphite powder with the particle size of 0.05-0.1mm, separated and escaped by airflow, is absorbed by the spray tower I, and volatilized ethylene carbonate enters the UV photolysis air purifier I through the dryer to be decomposed into carbon dioxide and water vapor to be discharged, so that environmental pollution can be effectively reduced;
the materials separated by the analyzer enter a swing sieve, the swing sieve is 50 meshes, positive and negative electrode materials can be screened out, the upper end of the swing sieve is connected with a pipeline, the pipeline guides the airflow of the analyzer to a collector III, dust in the collector III is conveyed to a pulse dust remover III for primary filtration, then the dust is conveyed to a spray tower II through a high-pressure induced draft fan III for secondary filtration, small molecular harmful gas is also present in the filtered airflow, the filtered airflow is subjected to tertiary filtration through a UV photolysis air purifier II, finally, completely harmless gas is obtained, the completely harmless gas is discharged outwards through the induced draft fan III, graphite powder with the particle size of 0.05-0.1mm is absorbed by the spray tower II, and volatilized ethylene carbonate enters the UV photolysis air purifier II through a dryer for decomposition into carbon dioxide and water vapor for removal, so that the environmental pollution can be effectively reduced;
the material screened by the swinging sieve enters a grinder, the material is ground to 100 meshes, the upper end of the grinder is connected with a pipeline, the pipeline guides the airflow of an analyzer to a collector IV, dust in the collector IV is conveyed to a pulse dust collector III for primary filtration, then the dust is conveyed to a spray tower II through a high-pressure induced draft fan III for secondary filtration, small molecular harmful gas is also present in the filtered airflow, the filtered airflow is subjected to tertiary filtration through a UV photolysis air purifier II, finally, completely harmless gas is obtained, the completely harmless gas is discharged outwards through the induced draft fan III, graphite powder with the particle size of 0.05-0.1mm is absorbed by the spray tower II in the process, and volatilized ethylene carbonate enters the UV photolysis air purifier II through a dryer for decomposition into carbon dioxide and water vapor for removal, so that the environmental pollution can be effectively reduced;
the ground materials enter a rotary vibration sieve and are sieved to obtain powder, wherein the main bodies of the powder are copper powder, aluminum powder, graphite powder and lithium cobaltate powder.
According to the pollution-free lithium battery decomposition treatment system provided by the application, a lithium battery is crushed by shredding, graphite powder, lithium cobaltate powder, diaphragm electrolyte, aluminum foil and copper foil are leaked out, the crushed lithium battery is fed into an airflow separator, ethylene carbonate volatilizes, lithium hexafluorophosphate is decomposed to obtain phosphorus fluoride and lithium fluoride, most of the phosphorus fluoride and most of the lithium fluoride enter a collector I along with a diaphragm, and the scattered phosphorus fluoride, lithium fluoride and graphite powder enter a spray tower I to avoid air pollution.
Finally, it should be noted that: the foregoing description is only illustrative of the preferred embodiments of the present application, and although the present application has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described, or equivalents may be substituted for elements thereof, and any modifications, equivalents, improvements or changes may be made without departing from the spirit and principles of the present application.

Claims (5)

1. A pollution-free lithium battery decomposition processing system is characterized in that: including shredder, breaker, air current sorter, magnetic separation conveyer, rubbing crusher, analytical engine, swinging screen, mill, the sieve that shakes soon that connects gradually, shredder and breaker all are connected to pulse dust remover I through the pipeline, the air current sorter is connected with collector I through draught fan II, collector I is connected to pulse dust remover I, pulse dust remover I is connected with first air purification device through high-pressure draught fan I, the analytical engine is connected to second air purification device through collector II, pulse dust remover II, high-pressure draught fan II that connect gradually, the swinging screen is connected with collector III, the mill is connected with collector IV, collector III and collector IV all are connected to pulse dust remover III, pulse dust remover III is connected to second air purification device through high-pressure draught fan III,
the first air purification device comprises a spray tower I connected with a high-pressure induced draft fan I, the spray tower I is connected with a UV photolysis air purifier I through a dryer I, the UV photolysis air purifier I is connected with the induced draft fan I,
the second air purification device comprises a spray tower II connected with a high-pressure induced draft fan II and a high-pressure induced draft fan II, wherein the spray tower II is connected with a UV photolysis air purifier II through a dryer I, and the UV photolysis air purifier II is connected with an induced draft fan III
The grinding granularity of the grinder is 20-30 meshes, the grinding granularity of the grinder is 80-100 meshes,
in the steel shell lithium battery, a shell is a steel shell, a positive plate is an aluminum foil, a negative plate is a copper foil, a positive electrode material is lithium cobaltate, a negative electrode material is graphite, a diaphragm is a high polymer film, an electrolyte is ethylene carbonate in which lithium hexafluorophosphate is dissolved, the battery is put into a shredder, the shredded battery falls into a shredder to be shredded, the diaphragm is scattered in the shredding process, the shredder and the shredder are operated, generated dust is conveyed to a pulse dust remover I through pipelines respectively arranged in the shredder and the shredder to be filtered for the first time, then conveyed to a spray tower I through a high-pressure induced draft fan I to be filtered for the second time, small molecular harmful gas is still present in the dried airflow after filtration, the third time is filtered through a UV photolysis air purifier I, finally, completely harmless gas is obtained and is discharged outwards through the induced draft fan I, and graphite powder with the particle size of 0.05-0.1mm generated by shredding and shredding is absorbed by the spray tower I in the process, and the volatilized ethylene carbonate enters the UV photolysis air purifier I through the dryer to be decomposed into carbon dioxide and water vapor;
the crushed batteries are conveyed to an airflow separator through a conveying belt, dust and scattered diaphragms are conveyed to a collector I through a draught fan II under the action of airflow and vibration, dust in the collector 1 is conveyed to a pulse dust collector I for primary filtration, then is conveyed to a spray tower II through a high-pressure draught fan I for secondary filtration, micromolecular harmful gas is still present in the filtered airflow, the filtered airflow is subjected to tertiary filtration through a UV photolysis air purifier I, finally, completely harmless gas is obtained, the completely harmless gas is discharged outwards through the draught fan I, graphite powder with the particle size of 0.05-0.1mm, which is separated and escaped by the airflow, is absorbed by the spray tower I, and volatilized ethylene carbonate enters the UV photolysis air purifier I through a dryer and is decomposed into carbon dioxide and water vapor for removal;
the method comprises the steps that materials which are not scattered in a battery in a crusher also enter a magnetic separation conveyor, crushed steel shells are separated, the separated materials enter the crusher to be crushed into 20-30 meshes, the crushed materials are conveyed to an analyzer, the upper end of the analyzer is connected with a pipeline, airflow of the analyzer is conveyed to a collector II through the pipeline, dust in the collector II is conveyed to a pulse dust collector II to be subjected to primary filtration, and then conveyed to a spray tower II through a high-pressure induced draft fan II to be subjected to secondary filtration, micromolecular harmful gases are also contained in the filtered airflow, the filtered airflow is subjected to tertiary filtration through a UV photolysis air purifier II, finally, completely harmless gases are obtained, the completely harmless gases are discharged outwards through a draft fan III, and graphite powder with the particle size of 0.05-0.1mm, separated and escaped by the airflow is absorbed by the spray tower I, and volatilized ethylene carbonate enters a UV photolysis air purifier I through a dryer to be decomposed into carbon dioxide and water vapor to be discharged;
the material separated by the analyzer enters a swing sieve, the swing sieve is 50 meshes, positive and negative electrode materials can be screened out, the upper end of the swing sieve is connected with a pipeline, the pipeline guides the airflow of the analyzer to a collector III, dust in the collector III is conveyed to a pulse dust remover III for primary filtration, then the dust is conveyed to a spray tower II through a high-pressure induced draft fan III for secondary filtration, small molecular harmful gas is also present in the filtered airflow, the filtered airflow is subjected to tertiary filtration through a UV photolysis air purifier II, finally, completely harmless gas is obtained, the completely harmless gas is discharged outwards through the induced draft fan III, graphite powder with the particle size of 0.05-0.1mm is absorbed by the spray tower II, and volatilized ethylene carbonate enters the UV photolysis air purifier II through a dryer for decomposition into carbon dioxide and water vapor for removal;
the material screened by the swinging sieve enters a grinder, the material is ground to 100 meshes, the upper end of the grinder is connected with a pipeline, the pipeline guides the airflow of an analyzer to a collector IV, dust in the collector IV is conveyed to a pulse dust collector III for primary filtration, then the dust is conveyed to a spray tower II through a high-pressure induced draft fan III for secondary filtration, small molecular harmful gas is also present in the filtered airflow, the filtered airflow is subjected to tertiary filtration through a UV photolysis air purifier II, finally, completely harmless gas is obtained, the completely harmless gas is discharged outwards through the induced draft fan III, graphite powder with the particle size of 0.05-0.1mm is absorbed by the spray tower II in the process, and volatilized ethylene carbonate enters the UV photolysis air purifier II through a dryer for decomposition into carbon dioxide and water vapor for removal;
the ground materials enter a rotary vibration sieve and are sieved to obtain powder, wherein the main bodies of the powder are copper powder, aluminum powder, graphite powder and lithium cobaltate powder.
2. The non-contaminating lithium battery decomposition treatment system of claim 1, wherein: the shredder comprises a frame I and a shell I positioned on the frame I, wherein a feed inlet I is formed in the upper end of the shell I, driving devices I are respectively arranged on two sides of the frame I, a rotating shaft I and a rotating shaft II which are connected with the driving devices I are respectively arranged on two sides in the shell I, blades are distributed on the rotating shaft I and the rotating shaft II in a circumferential manner, spacers are arranged between adjacent blades, the blades on the rotating shaft I and the rotating shaft II are arranged in a staggered mode, and a discharge outlet II is formed in the lower end of the shell I.
3. The non-contaminating lithium battery decomposition treatment system of claim 1, wherein: the crusher comprises a frame II, a shell II and a driving device II, wherein the shell II and the driving device II are arranged on the frame II, a feed inlet II is formed in one side of the upper end of the shell II, a crushing mechanism is arranged in the shell II and comprises a rotating shaft III, a fixing rod and a hammer head, the rotating shaft III is connected with the driving device II through a belt, the fixing rods are uniformly distributed on the circumference of the rotating shaft III and comprise n baffle plates perpendicular to the axis of the rotating shaft III and connecting rods penetrating through the end parts of the baffle plates, and the hammer head is sleeved on the connecting rods; the lower extreme of crushing mechanism is provided with the filter screen, the lower extreme of casing II is provided with the export.
4. The non-contaminating lithium battery decomposition treatment system of claim 3, wherein: the hammer head is located on the connecting rod between the adjacent partition boards, a limiting block matched with the width of the hammer head is arranged on the connecting rod, and the distance from the connecting rod to the rotating shaft III is larger than the length of the hammer head.
5. The non-contaminating lithium battery decomposition treatment system of claim 1, wherein: cyclone dust collectors are selected from the collector I, the collector II, the collector III and the collector IV.
CN201811321379.0A 2018-11-07 2018-11-07 Pollution-free lithium battery decomposition treatment system Active CN109256600B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811321379.0A CN109256600B (en) 2018-11-07 2018-11-07 Pollution-free lithium battery decomposition treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811321379.0A CN109256600B (en) 2018-11-07 2018-11-07 Pollution-free lithium battery decomposition treatment system

Publications (2)

Publication Number Publication Date
CN109256600A CN109256600A (en) 2019-01-22
CN109256600B true CN109256600B (en) 2023-10-20

Family

ID=65044667

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811321379.0A Active CN109256600B (en) 2018-11-07 2018-11-07 Pollution-free lithium battery decomposition treatment system

Country Status (1)

Country Link
CN (1) CN109256600B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112058872A (en) * 2020-09-03 2020-12-11 河北大学 Device and method for crushing and sorting solar cell modules
CN112290111A (en) * 2020-12-01 2021-01-29 苏州兮然工业设备有限公司 Lithium battery recovery process

Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101984516A (en) * 2010-08-19 2011-03-09 江苏锐毕利实业有限公司 Lithium ion battery resource recovery method for mobile phones
JP2014049257A (en) * 2012-08-30 2014-03-17 Miura Co Ltd High temperature type fuel cell system
CN106140796A (en) * 2016-08-25 2016-11-23 巩义市城区润达机械厂 Useless lithium battery processing system and process technique
CN205926578U (en) * 2016-08-25 2017-02-08 巩义市城区润达机械厂 Useless lithium battery processing system
CN107413192A (en) * 2017-08-01 2017-12-01 陶洋 A kind of emission-control equipment of painting dressing automobiles
CN207169404U (en) * 2017-08-25 2018-04-03 武汉坤久环保科技有限公司 A kind of waste gas purification apparatus for old and useless battery extraction plant
CN108011148A (en) * 2017-11-29 2018-05-08 河南小威环境科技有限公司 A kind of method from waste and old lithium ion battery recycling metal
CN108114584A (en) * 2018-02-10 2018-06-05 清远韶兴新能源科技有限公司 A kind of industrial emission-control equipment
CN108114969A (en) * 2018-02-02 2018-06-05 广州中国科学院沈阳自动化研究所分所 Power battery monomer harmless disassembly separation platform and method
CN207572492U (en) * 2017-12-08 2018-07-03 天齐锂业股份有限公司 A kind of full-automatic waste and old lithium ion battery recovery system
CN108258357A (en) * 2018-03-31 2018-07-06 巩义市城区润达机械厂 A kind of lithium battery processing system and treatment process
CN108336440A (en) * 2018-01-05 2018-07-27 深圳市比克电池有限公司 A kind of waste and old lithium ion battery collector recovery method
CN207680267U (en) * 2017-10-31 2018-08-03 成都晟蓝环保科技有限公司 A kind of industrial waste gas purifying system based on UV photodissociation and plasma decomposition
CN108615956A (en) * 2018-06-14 2018-10-02 河南巨峰环保科技有限公司 A kind of electric discharge dynamic lithium battery recovery process
CN209200110U (en) * 2018-11-07 2019-08-02 巩义市城区润达机械厂 Pollution-free lithium battery resolution process system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160045841A1 (en) * 2013-03-15 2016-02-18 Transtar Group, Ltd. New and improved system for processing various chemicals and materials

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101984516A (en) * 2010-08-19 2011-03-09 江苏锐毕利实业有限公司 Lithium ion battery resource recovery method for mobile phones
JP2014049257A (en) * 2012-08-30 2014-03-17 Miura Co Ltd High temperature type fuel cell system
CN106140796A (en) * 2016-08-25 2016-11-23 巩义市城区润达机械厂 Useless lithium battery processing system and process technique
CN205926578U (en) * 2016-08-25 2017-02-08 巩义市城区润达机械厂 Useless lithium battery processing system
CN107413192A (en) * 2017-08-01 2017-12-01 陶洋 A kind of emission-control equipment of painting dressing automobiles
CN207169404U (en) * 2017-08-25 2018-04-03 武汉坤久环保科技有限公司 A kind of waste gas purification apparatus for old and useless battery extraction plant
CN207680267U (en) * 2017-10-31 2018-08-03 成都晟蓝环保科技有限公司 A kind of industrial waste gas purifying system based on UV photodissociation and plasma decomposition
CN108011148A (en) * 2017-11-29 2018-05-08 河南小威环境科技有限公司 A kind of method from waste and old lithium ion battery recycling metal
CN207572492U (en) * 2017-12-08 2018-07-03 天齐锂业股份有限公司 A kind of full-automatic waste and old lithium ion battery recovery system
CN108336440A (en) * 2018-01-05 2018-07-27 深圳市比克电池有限公司 A kind of waste and old lithium ion battery collector recovery method
CN108114969A (en) * 2018-02-02 2018-06-05 广州中国科学院沈阳自动化研究所分所 Power battery monomer harmless disassembly separation platform and method
CN108114584A (en) * 2018-02-10 2018-06-05 清远韶兴新能源科技有限公司 A kind of industrial emission-control equipment
CN108258357A (en) * 2018-03-31 2018-07-06 巩义市城区润达机械厂 A kind of lithium battery processing system and treatment process
CN108615956A (en) * 2018-06-14 2018-10-02 河南巨峰环保科技有限公司 A kind of electric discharge dynamic lithium battery recovery process
CN209200110U (en) * 2018-11-07 2019-08-02 巩义市城区润达机械厂 Pollution-free lithium battery resolution process system

Also Published As

Publication number Publication date
CN109256600A (en) 2019-01-22

Similar Documents

Publication Publication Date Title
CN108258357B (en) Lithium battery treatment system and treatment process
CN110571306B (en) Photovoltaic module recycling method and system
CN108110356B (en) Full-automatic waste lithium ion battery recycling process and system
CN111530884B (en) Power lithium battery monomer recovery method
CN105826629A (en) All-component material separation and collection device and method for waste lithium batteries
CN105811040A (en) Method for smashing, detaching and recycling lithium battery
CN109985714A (en) It is a kind of for screening the device and its technique of black powder and copper aluminium in old and useless battery
CN205609702U (en) Old and useless lithium cell complete set divides material separation collection device
CN109256600B (en) Pollution-free lithium battery decomposition treatment system
CN111872021A (en) Environment-friendly waste lithium battery recovery processing system
CN112275765B (en) Method for treating waste lithium battery diaphragm paper
CN111525209B (en) Recovery method of power lithium battery
CN111097586A (en) Broken production system that retrieves of high electric quantity lithium cell
CN215933683U (en) Multichannel waste lithium battery electrified disassembling and recycling equipment
CN115149138A (en) Waste lithium battery disassembling and recycling device and method
CN209200110U (en) Pollution-free lithium battery resolution process system
CN112201872B (en) Safe discharge method and wet physical sorting method for retired batteries
CN211629249U (en) Broken production line of retrieving of lithium cell positive plate
CN202951700U (en) Waste belt component circuit board treatment device
CN208208918U (en) A kind of dismantling recovery system of waste lithium cell
CN111146523A (en) Disassembling, classifying and recycling process method for waste batteries
CN207929286U (en) A kind of integrated apparatus sorted suitable for building waste with crushing
CN217158305U (en) Vehicle-mounted safe crushing and recycling device for waste lithium batteries
CN209997754U (en) device for screening black powder and copper and aluminum in waste batteries
CN113083862B (en) Dry pole piece treatment and recovery system with diaphragm and method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20200417

Address after: No.23, building e, industrial cluster, Huiguo Town, Gongyi City, Zhengzhou City, Henan Province 451200

Applicant after: Gongyi Jixin Machinery Co.,Ltd.

Address before: 451200, Zhengzhou, Henan, Gongyi province Xiaoyi Street filial piety North Village

Applicant before: GONGYI CITY RUNDA MACHINERY FACTORY

GR01 Patent grant
GR01 Patent grant