CN216354402U

CN216354402U - Economical ternary lithium battery disassembling and recycling system

Info

Publication number: CN216354402U
Application number: CN202122877529.XU
Authority: CN
Inventors: 孙庆斌
Original assignee: Luyue Automation Technology Shanghai Co ltd
Current assignee: Luyue Automation Technology Shanghai Co ltd
Priority date: 2021-11-19
Filing date: 2021-11-19
Publication date: 2022-04-19
Anticipated expiration: 2031-11-19

Abstract

The utility model discloses an economical ternary lithium battery disassembling and recycling system, which is characterized in that a uniform feeder, a belt conveyor line I, a primary crusher, a secondary crusher, a tertiary crusher and a winnowing system are sequentially connected, the winnowing system is respectively connected with a powder remover and one end of the belt conveyor line, the other end of the powder remover is respectively connected with a cyclone separator and a linear sieve, the outlet of the winnowing system is connected with a combined magnetic separator, an eddy current separator, a belt conveyor line IV, a quaternary crusher, a linear sieve II, a belt conveyor line V and a distributor through a belt conveyor line II and a belt conveyor line III, the powder remover and the cyclone separator are respectively connected with one end of a black powder dynamic heating bin, and the other end of the black powder dynamic heating bin I is sequentially connected with the black powder dynamic heating bin II, a high-temperature rotary kiln and a black powder negative pressure collecting bin. Introducing a nitrogen protection system and a negative pressure dust removal system to ensure the safety coefficient of a production line; and a dynamic storage bin is introduced to replace a heating kiln, so that the energy consumption is reduced and the economic benefit is improved.

Description

Economical ternary lithium battery disassembling and recycling system

Technical Field

The utility model relates to the technical field of disassembly and recovery of ternary lithium batteries, in particular to an economical disassembly and recovery system of ternary lithium batteries.

Background

The lithium ion battery has the advantages of high energy, long service life, low pollution and the like, and is widely applied to collection, computers, electric bicycles, electric automobiles, national defense and the likeA field of application. Especially, in recent years, the explosive growth of electric automobiles and the accompanying large-scale power lithium battery market have the problem that the demand and the scrap quantity of lithium batteries are greatly increased. The waste lithium ion batteries contain a large amount of available resources, such as valuable metals like iron, copper, aluminum, etc., and if the waste lithium batteries are improperly recovered, great resource waste and environmental pollution can be caused. Meanwhile, substances such as anode and cathode materials and electrolyte solution of the lithium ion battery have great influence on the environment and human health. Therefore, if the waste lithium battery is treated by a common garbage treatment method (including landfill, incineration, composting and the like), metals such as nickel, cobalt, manganese, lithium and the like in the anode and cathode materials cause heavy metal pollution to water and soil. And an electrolyte and a converted substance thereof such as LiPF₆、LiCF₃SO₃、 HF、P₂O₅And the solvent and its decomposition and hydrolysis products such as DME, EMC, methanol, formic acid, etc. are toxic and harmful substances, which can cause personal injury and even death.

On the other hand, the demand of lithium batteries is increased explosively, taking metal lithium as an example, in 2050 years, the global demand of metal lithium is predicted to reach 4000 ten thousand tons, the global metal lithium resource is at most 3000 ten thousand tons at present, it is proved that only 1500 ten thousand tons of lithium ore resources can be utilized, and huge gaps exist between supply and demand, so that the price of upstream raw materials is increased rapidly, the cost and pressure of lithium battery manufacturers are increased dramatically, and the recycling of lithium batteries is a necessary trend.

The current policy of recycling guides that the waste batteries are encouraged to be recycled in a gradient mode and then disassembled and recycled so as to give full play to the economic benefits of the waste batteries, but the gradient utilization is limited by the uniformity and the cost influence of the batteries, the quantity of the current gradient utilization is small, or the disassembly and recycling are mainly used, wherein the most valuable materials are anode and cathode materials and current collectors (copper/aluminum).

The disassembly and recovery of the lithium battery can be divided into dry recovery (physical method), hydrometallurgical recovery and biological recovery according to the principle, and the dry recovery is the mainstream at present.

The physical method for disassembling and recovering the lithium battery mainly adopts manual disassembly at first, has low efficiency and low recovery rate, and various toxic substances harm the safety of human bodies, and gradually develops to a process route of mechanical crushing and mechanical screening in the later period, and valuable anode and cathode materials and current collectors are extracted by combining with hydrometallurgy in the later period.

The prior art is as follows: the current common dismantling and recycling technology in the market mainly follows the following route: deep discharge → primary crushing → secondary crushing → primary screening → tertiary crushing → secondary screening → magnetic separation → air current separation → high temperature burning → collection → hydrometallurgical refining.

(1) The safety is insufficient: the lithium battery needs to be deeply discharged until the residual electric energy is below 10% of cut-off voltage before crushing, but a part of electric energy can be recovered after transportation and storage for a certain time, and the risk of fire and explosion can be caused by charged crushing; the electrolyte released in the crushing process reaches a certain concentration inside the equipment and is easy to ignite and explode, and meanwhile, the electrolyte also has strong corrosivity on the equipment and has certain influence on the service life and the safety of the equipment.

(2) The recovery rate is not high: the process only collects metal substances with higher recovery value and positive and negative electrode materials, and directly burns the electrolyte and the diaphragm, thereby increasing the energy consumption and the load of a tail gas treatment system.

(3) The recovery precision is not high: the positive and negative electrode materials are coated on the surfaces of the positive and negative electrode current collectors through binders and are difficult to completely strip out through conventional crushing, the positive and negative electrode materials and copper-aluminum fine powder which fall off in the crushing process are mutually doped together under the action of a wet electrolyte, and finally, the purity of the positive and negative electrode materials, copper and aluminum obtained through separation is not high.

(4) Production continuity problems: in the process, the linkage among the devices is not strong, once one device fails, the whole production line cannot be immediately shut down, if the residual materials in the device are too much, the device can be damaged, the production line can be restarted after the cleaning is finished, and the time for recovering the production of the production line is long.

(5) The environmental pollution is serious: the dust leakage in the crushing process causes poor field environment, and the high-temperature incineration of electrolyte, a diaphragm, a binder and the like causes standard exceeding of various harmful substances in tail gas and environmental pollution.

(6) The economic benefit problem is as follows: aiming at a production line with low capacity, if a complete crushing and disassembling recovery system is adopted, the energy consumption is too high, and the input-output ratio cannot reach the expected value.

SUMMERY OF THE UTILITY MODEL

The utility model aims to provide an economical ternary lithium battery disassembling and recycling system to solve the problems in the background technology.

In order to achieve the purpose, the utility model provides the following technical scheme: an economical ternary lithium battery disassembling and recycling system comprises a uniform feeder, a belt conveyor line I, a primary crusher, a secondary crusher, a tertiary crusher, a winnowing system, a belt conveyor line II, a powder remover, a cyclone separator, a linear sieve I, a black powder dynamic heating bin I, a belt conveyor line III, a combined magnetic separator, an eddy current separator, a belt conveyor line IV, a secondary crusher, a linear sieve II, a belt conveyor line V, a distributor, a copper-aluminum separation system, a bag-type dust remover I, a bag-type dust remover II, an electrolyte volatilizing and condensing device, a bag-type dust remover III, an electrolyte storage tank, a black powder dynamic heating bin II, a high-temperature rotary kiln, a black powder negative pressure collection bin, a secondary combustion chamber, a flue gas cooler, an alkali liquor spraying device I, an alkali liquor spraying device II, an active carbon adsorption device, a draught fan I, a discharge chimney, a draught fan II, a heat exchanger and an alkali liquor spraying device III, the uniform feeder, belt conveyor line one, primary crusher, secondary crusher, tertiary crusher, air classification system connects gradually, air classification system is connected with the one end of taking off powder ware and belt conveyor line respectively, the other end of taking off the powder ware is connected with cyclone and sharp sieve respectively, the air classification system export is through belt conveyor line two, belt conveyor line three and combination formula magnet separator, eddy current sorter, belt conveyor line four, secondary crusher, sharp sieve two, belt conveyor line five and tripper are connected, the tripper is connected with copper aluminium sorting system, powder remover and cyclone all are connected with black powder dynamic heating feed bin one end, the other end of black powder dynamic heating feed bin one in proper order with black powder dynamic heating feed bin two, high temperature rotary kiln and black powder negative pressure collection storehouse are connected.

Preferably, the copper-aluminum sorting system is two sets of same equipment, and all contains primary copper-aluminum sorter, bucket elevator, five-time crusher, vibration disc screen, secondary copper-aluminum sorter, copper grain ton package collection and aluminum grain negative pressure collection feed bin, and primary copper-aluminum sorter, bucket elevator, five-time crusher, vibration disc screen and secondary copper-aluminum sorter connect gradually the setting, and secondary copper-aluminum sorter is connected with copper grain collection ton package and aluminum grain negative pressure collection feed bin respectively.

Preferably, the first bag-type dust collector, the second bag-type dust collector, the electrolyte volatilization condensing device, the third bag-type dust collector, the second combustion chamber, the flue gas cooler, the first alkali liquor spraying device, the second alkali liquor spraying device, the activated carbon adsorption device, the first draught fan, the emission chimney, the second draught fan and the alkali liquor spraying device form a tail gas recovery system.

Preferably, primary crusher, secondary crusher, tertiary crusher, cyclone, all be connected with tail gas recovery system through the tail gas pipeline, sack cleaner one is connected with the condensing equipment that volatilizees of electrolyte, the condensing equipment that volatilizees of electrolyte is connected with the one end of condensation component storage jar and sack cleaner three respectively, the other end and the second combustion chamber of sack cleaner three are connected, the top and the heat exchanger of second combustion chamber are connected, the bottom of second combustion chamber respectively with the flue gas cooler, alkali lye spray set one, alkali lye spray set two, active carbon adsorption device, draught fan one, the emission chimney connects gradually.

Compared with the prior art, the system introduces a nitrogen protection system and a negative pressure dust removal system, and ensures the safety coefficient of a production line; a dynamic storage bin is introduced to replace a heating kiln, so that the energy consumption is reduced and the economic benefit is improved; the powder remover and the multiple groups of sorting devices which are developed exclusively improve the material separation efficiency, and the diaphragm collecting and electrolyte collecting devices are arranged, so that the utilization rate of the waste batteries is improved;

the utility model has the following beneficial effects: 1. the dust leakage possibility is low, the production line environment is ensured, and the production line safety coefficient is improved.

2. The production line is controlled in a centralized way, the process and state control is enhanced, excessive manual participation is not needed, and the labor cost is saved;

3. the process route is simplified: after the two primary crushing, removing the binder from the material by a high-temperature rotary kiln, separating the current collector aluminum foil and the positive active material by a powder remover and a linear screen, if the requirement on the purity of the positive active material is not high, crushing and screening are not needed again, secondary crushing, screening and recycling can be carried out if the requirement is high, the process route is simple, the number of equipment is reduced, and the energy consumption is reduced;

4. the recovery purity of each component is high;

5. the dust gas treated by the tail gas treatment system can reach the emission standard of the local hazardous waste incineration pollution control standard, and no tail gas treatment equipment is additionally arranged.

Drawings

FIG. 1 is a schematic diagram of the recycling system of the present invention.

In the figure: the device comprises a uniform feeder c, a belt conveyor line I1-1, a primary crusher 2, a secondary crusher 3, a tertiary crusher 4, a winnowing system a, a belt conveyor line II 1-2, a powder remover 5, a cyclone separator 6, a linear screen I, a belt conveyor line III 1-3, a black powder dynamic heating bin I8, a combined magnetic separator 9, an eddy current separator 10, a belt conveyor line IV 1-4, 11, a secondary crusher 12, a linear screen II 13, a belt conveyor line V1-5, a distributor 14, a copper-aluminum separation system, a bag-type dust collector I16, a bag-type dust collector II 17, an electrolyte volatilization and condensation device 18, a bag-type dust collector III 19, an electrolyte storage tank 20, a black powder dynamic heating bin II 21, a high-temperature rotary kiln 22, a black powder negative pressure collection bin 23, a secondary combustion chamber 24, a flue gas cooler 25, an alkali liquor spraying device I26, a, 26-1 parts of a second alkali liquor spraying device, 27 parts of an activated carbon adsorption device, 28 parts of a heat exchanger, 29 parts of a third alkali liquor spraying device, 15-1 parts of a primary copper-aluminum separator, 15-2 parts of a bucket elevator, 15-3 parts of a five-time crusher, 15-4 parts of a vibrating disc screen, 15-5 parts of a secondary copper-aluminum separator, 15-6 parts of an aluminum particle negative pressure collecting bin, a draught fan d1, a draught fan d2 and a discharge chimney d 3.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

Referring to fig. 1, the present invention provides a technical solution: an economical ternary lithium battery disassembling and recycling system comprises a uniform feeder c, a belt conveyor line I1-1, a primary crusher 2, a secondary crusher 3, a secondary crusher 4, a winnowing system a, a belt conveyor line II 1-2, a powder remover 5, a cyclone separator 6, a linear sieve I7, a black powder dynamic heating bin I8, a belt conveyor line III 1-3, a combined magnetic separator 9, an eddy current separator 10, a belt conveyor line IV 1-4, a secondary crusher 12, a linear sieve II 13, a belt conveyor line V1-5, a distributor 14, a copper-aluminum separation system, a bag-type dust remover I16, a bag-type dust remover II 17, an electrolyte volatilization and condensation device 18, a bag-type dust remover III 19, an electrolyte storage tank 20, a black powder dynamic heating bin II 21, a high-temperature rotary kiln 22, a black powder negative pressure collection bin 23, a secondary combustion chamber 24, The device comprises a flue gas cooler 25, an alkali liquor spraying device I26, an alkali liquor spraying device II 26-1, an activated carbon adsorption device 27, an induced draft fan d1, a discharge chimney d3, an induced draft fan II d2, a heat exchanger 28 and an alkali liquor spraying device III 29, wherein a uniform feeder c, a belt conveying line I1-1, a primary crusher 2, a secondary crusher 3, a tertiary crusher 4 and a winnowing system a are sequentially connected, the winnowing system a is respectively connected with a powder remover 5 and one end of the belt conveying line, the other end of the powder remover 5 is respectively connected with a cyclone separator 6 and a linear sieve I7, an outlet of the winnowing system a is connected with a combined magnetic separator 9, a vortex current separator 10, a belt conveying line IV 1-4, a secondary crusher 12, a linear sieve II 13, a belt conveying line IV 1-5 and a distributor 14 through the belt conveying line II 1-2 and the belt conveying line III 3, the distributor 14 is connected with a copper-aluminum sorting system, the powder remover 5 and the cyclone separator 6 are both connected with one end of a first black powder dynamic heating bin 8, and the other end of the first black powder dynamic heating bin 8 is sequentially connected with a second black powder dynamic heating bin 21, a high-temperature rotary kiln 22 and a black powder negative pressure collecting bin 23.

Preferably, the copper-aluminum sorting system comprises two sets of same equipment, and each set of equipment comprises a primary copper-aluminum sorting machine 15-1, a bucket elevator 15-2, a five-time crusher 15-3, a vibration disc screen 15-4, a secondary copper-aluminum sorting machine 15-5, a copper particle ton bag collecting and aluminum particle negative pressure collecting bin 15-6, the primary copper-aluminum sorting machine 15-1, the bucket elevator 15-2, the five-time crusher 15-3, the vibration disc screen 15-4 and the secondary copper-aluminum sorting machine 15-5 are sequentially connected, and the secondary copper-aluminum sorting machine 15-5 is respectively connected with the copper particle collection ton bag and the aluminum particle negative pressure collecting bin 15-6.

Preferably, the tail gas recovery system is composed of a first bag-type dust collector 16, a second bag-type dust collector 17, an electrolyte volatilization and condensation device 18, a third bag-type dust collector 19, a second combustion chamber 24, a flue gas cooler 25, a first alkali liquor spraying device 26, a second alkali liquor spraying device 26-1, an activated carbon adsorption device 27, a first induced draft fan d1, a discharge chimney d3, a second induced draft fan d2 and a third alkali liquor spraying device 29.

Preferably, the primary crusher 2, the secondary crusher 3, the tertiary crusher 4 and the cyclone separator 6 are all connected with a tail gas recovery system through a tail gas pipeline, the first bag-type dust collector 16 is connected with the electrolyte volatilization condensing device 18, the electrolyte volatilization condensing device 18 is respectively connected with one end of a condensation component storage tank 20 and one end of a bag-type dust collector three 19, the other end of the bag-type dust collector three 19 is connected with the second combustion chamber 24, the top of the second combustion chamber 24 is connected with the heat exchanger 28, the bottom of the second combustion chamber 24 is respectively connected with the flue gas cooler 25, the first alkali liquor spraying device 26, the second alkali liquor spraying device 26-1, the activated carbon adsorption device 17 and the first draft fan d1 discharge chimney d3 in sequence.

An economical method for disassembling and recycling a ternary lithium battery comprises the following steps: step one, raw material waste batteries are hung to a unpacking platform through an electric hoist, the waste batteries are put into a bin through manual unpacking, the batteries are conveyed to a vibrating feeder through a chain plate at a constant speed and are evenly put on a belt conveyor line I1-1, the waste batteries are conveyed to a primary crusher 2, the crushed waste batteries enter a secondary crusher 3 after being crushed, large crushed objects are secondarily crushed, the crushed objects enter a tertiary crusher 4 and then are subjected to multi-component sorting and separation through a winnowing system a to obtain a steel shell, a diaphragm, black powder and positive and negative pole pieces enter a powder remover 5 to separate the black powder, oversize products enter a linear sieve I7 to continuously separate the black powder, the black powder separated by the powder remover 5 and the linear sieve I7 is intensively collected into a black powder dynamic heating bin I8 through a negative pressure conveying system, the oversize products are the positive and negative pole pieces and a small amount of diaphragm, and the oversize products enter a combined magnetic separator 9 together with the winnowing steel shell to separate magnetic substances and are separately collected, a large number of plastic pieces in the waste batteries can be separated out by the eddy current separator 10 and collected independently, and the rest materials enter the four-time crusher 12 through the belt conveyor to be crushed; the waste batteries are protected by nitrogen gas from the primary crushing to the tertiary crushing, so that the dangers of fire explosion and the like caused by crushing are prevented;

after the second crushing and the fourth crushing, separating black powder falling off in the crushing process by a linear sieve II 13, conveying the black powder into a black powder dynamic heating bin I8 through negative pressure, uniformly distributing materials on a sieve by a distributor 14, and then falling into two sets of copper and aluminum sorting systems to perform primary sorting on copper and aluminum;

step three, conveying copper foil to a five-time crusher 15-3 through a belt conveyor and a bucket elevator 15-2 at a copper outlet of the copper-aluminum sorting system, separating foreign matters by falling into a vibration disc sieve 15-4 after crushing, finely sorting oversize matters in a secondary copper-aluminum sorting machine 15-5 through a layer of sieve, collecting copper foil by a ton bag, and collecting aluminum particles by an aluminum particle negative pressure collecting bin 15-6; conveying the undersize black powder to a first black powder dynamic heating bin 8 through negative pressure, and carrying out the same operation steps by two copper-aluminum sorting systems;

step four, the black powder dynamic heating bin 8 is a dynamic stirring heating bin, the black powder separated in all links is intensively collected into the bin through negative pressure conveying, electrolyte doped in the black powder is volatilized in the heating and stirring processes, volatilized electrolyte tail gas is intensively collected through a tail gas pipeline and is condensed and collected through an electrolyte volatilization condensing device 18, if the production line capacity is large, a set of dynamic bin can be added at the front end of the dynamic bin to serve as a buffer for safety, all the collected black powder is pretreated in a cache bin to volatilize a part of electrolyte, the volatilization efficiency of the dynamic bin is improved, the black powder in the bin is ensured to volatilize the electrolyte and then enters the high-temperature rotary kiln 22 to be heated and roasted, a rotary cylinder body heated in the high-temperature rotary kiln 22 gradually conveys the material to the tail of the kiln bin from a high point to be cooled and then to be discharged under the actions of rotation, height difference and a lifting plate, the rotary cylinder is heated in a balanced manner, the heated cylinder conducts heat energy to the materials to achieve the purpose of roasting the materials, the generated waste gas is recovered by a tail gas recovery system and is discharged after qualified treatment, and the roasted materials are conveyed to a negative pressure collecting bin 23 by a negative pressure vacuum conveyor and are stored and packaged;

step five, the electrolyte tail gas respectively discharged from the black powder dynamic heating bin II 21 and the high-temperature rotary kiln 22 is firstly cooled, condensed and collected through the electrolyte volatilization condensing device 18, dust gas and other tail gas which cannot be collected are subjected to high-temperature treatment in the secondary combustion chamber 24 and then are prevented from being generated by dioxin through the flue gas cooler 25, and the treated tail gas is sprayed by alkali liquor of the alkali liquor spraying device I26 and the alkali liquor spraying device II 26-1 to remove HF and P and then is adsorbed by the activated carbon adsorption device 27, so that the emission standard of the environmental protection requirement is met, and the tail gas is naturally discharged.

Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that various changes in the embodiments and/or modifications of the utility model can be made, and equivalents and modifications of some features of the utility model can be made without departing from the spirit and scope of the utility model.

Claims

1. The utility model provides a recovery system is disassembled to economic ternary lithium cell which characterized in that: comprises a uniform feeder, a belt conveyor line I, a primary crusher, a secondary crusher, a tertiary crusher, a winnowing system, a belt conveyor line II, a powder remover, a cyclone separator, a linear sieve I, a black powder dynamic heating bin I, a belt conveyor line III, a combined magnetic separator, an eddy current separator, a belt conveyor line IV, a secondary crusher, a linear sieve II, a belt conveyor line V, a distributor, a copper-aluminum separation system, a bag-type dust remover I, a bag-type dust remover II, an electrolyte volatilization condensing device, a bag-type dust remover III, an electrolyte storage tank, a black powder dynamic heating bin II, a high-temperature rotary kiln, a black powder negative pressure collection bin, a secondary combustion chamber, a flue gas cooler, an alkali liquor spraying device I, an alkali liquor spraying device II, an active carbon adsorption device, a draught fan I, a discharge chimney, a draught fan II, a heat exchanger and an alkali liquor spraying device III, wherein the uniform feeder, the primary crusher, the secondary crusher, the belt conveyor line II, the powder remover, the cyclone separator, the linear sieve, the copper-aluminum separator, the copper separator, the aluminum separator, the copper separator, the aluminum separator, the device comprises a belt conveyor line I, a primary crusher, a secondary crusher, a tertiary crusher and a winnowing system which are sequentially connected, wherein the winnowing system is respectively connected with one end of a powder remover and one end of the belt conveyor line, the other end of the powder remover is respectively connected with a cyclone separator and a linear sieve, the outlet of the winnowing system is connected with a combined magnetic separator, a vortex current separator, a belt conveyor line IV, a secondary crusher, a linear sieve II, a belt conveyor line V and a distributor through a belt conveyor line II, the distributor is connected with a copper-aluminum separation system, the powder remover and the cyclone separator are respectively connected with a black powder dynamic heating bin one end, and the other end of the black powder dynamic heating bin I is sequentially connected with a black powder dynamic heating bin II, a high-temperature rotary kiln and a black powder negative pressure collecting bin.

2. The economical disassembly and recovery system for the ternary lithium battery as claimed in claim 1, wherein: the copper-aluminum sorting system comprises two sets of same equipment, and comprises a primary copper-aluminum sorting machine, a bucket elevator, a five-time crusher, a vibration disc sieve, a secondary copper-aluminum sorting machine, a copper particle ton bag collecting bin and an aluminum particle negative pressure collecting bin, wherein the primary copper-aluminum sorting machine, the bucket elevator, the five-time crusher, the vibration disc sieve and the secondary copper-aluminum sorting machine are sequentially connected, and the secondary copper-aluminum sorting machine is respectively connected with the copper particle collecting ton bag and the aluminum particle negative pressure collecting bin.

3. The economical disassembly and recovery system for the ternary lithium battery as claimed in claim 1, wherein: the tail gas recovery system is composed of a bag-type dust collector I, a bag-type dust collector II, an electrolyte volatilization condensing device, a bag-type dust collector III, a secondary combustion chamber, a flue gas cooler, an alkali liquor spraying device I, an alkali liquor spraying device II, an active carbon adsorption device, a draught fan I, a discharge chimney, a draught fan II and an alkali liquor spraying device.

4. The economical disassembly and recovery system for the ternary lithium battery as claimed in claim 1, wherein: primary crusher, secondary crusher, tertiary crusher, cyclone, all be connected with tail gas recovery system through the tail gas pipeline, sack cleaner one is connected with the condensing equipment that volatilizees of electrolyte, the condensing equipment that volatilizees of electrolyte is connected with the one end of condensation component storage jar and sack cleaner three respectively, the other end and the second combustion chamber of sack cleaner three are connected, the top and the heat exchanger of second combustion chamber are connected, the bottom of second combustion chamber respectively with the gas cooler, alkali lye spray set one, alkali lye spray set two, active carbon adsorption device, draught fan one, the emission chimney connects gradually.