Mobile device for treating lithium ion accumulators and method for treating lithium ion accumulators

Abstract

To provide a device for treating a lithium ion accumulator.SOLUTION: The invention relates to a movable type device for treating a lithium ion accumulator and a method for treating a lithium ion accumulator.SELECTED DRAWING: Figure 1

Description

[Technical field]

[0001] The present invention relates to a mobile device for treating a lithium-ion accumulator and a method for treating a lithium-ion accumulator. [Background technology]

[0002] Lithium-ion accumulators are a general term for accumulators based on lithium compounds. Such lithium-ion accumulators are also called lithium-ion accumulators or lithium-ion batteries. Due to their high specific energy, lithium-ion accumulators are used today in a variety of devices, such as smartphones, power tools, power gardening equipment, electric scooters, electric bicycles, electric forklifts, electric vehicles, stationary storage batteries or other applications in the field of electromobility.

[0003] At the end of the life of the lithium-ion accumulator, it is advisable for ecological and economic reasons to recover many of the raw materials present in the lithium-ion accumulator, such as lithium, cobalt, manganese, nickel, zinc, aluminum or copper. The same applies to the waste from the production of lithium-ion accumulators. In accordance with legal regulations, there is also an obligation for manufacturers or distributors of lithium-ion accumulators to take back the lithium-ion accumulators, although in part, so that the raw materials contained therein can be recycled.

[0004] A pre-treatment of lithium-ion accumulators is necessary so that the raw materials present in them can be recovered and recycled. Such treatment is usually carried out in factories specially designed for this purpose. To treat the lithium-ion accumulators in such factories with the aim of recovering the raw materials present in them, the lithium-ion accumulators are first collected by companies and public institutions and then transported in bulk to factories where they are treated. However, such transportation is associated with high costs. Furthermore, such transportation of lithium-ion accumulators involves safety risks due to the high risk of combustion and fire of lithium-ion accumulators. For this reason, for example, according to the "European Agreement concerning the International Carriage of Dangerous Goods by Road" (ADR), any transportation of lithium-ion accumulators is considered as a dangerous goods transportation, subject to special safety regulations. Summary of the Invention [Problem to be solved by the invention]

[0005] It is an object of the present invention to provide an apparatus for treating lithium ion accumulators, in particular capable of treating the lithium ion accumulators in such a way that the substances present in the lithium ion accumulators can then be recovered and such transport of the lithium ion accumulators can be reduced.

[0006] In particular, it is an object of the present invention to provide a mobile device for processing lithium ion accumulators. In doing so, the invention starts from the fundamental consideration of reducing the transportation of lithium ion accumulators to a device for processing the lithium ion accumulators by not transporting the lithium ion accumulators to the device but rather by transporting the device to the lithium ion accumulator for processing the lithium ion accumulator by the device. It is therefore also a particular object of the present invention to provide a device for processing lithium ion accumulators that is mobile such that it can be transported to the lithium ion accumulator. [Means for solving the problem]

[0007] To achieve these objects, according to the invention, a mobile device for processing lithium-ion accumulators is provided, which has the following characteristics: an input chamber, the lithium ion accumulator being receivable within the input chamber; a crushing device, the lithium ion accumulator received in the input chamber can be transported from the input chamber to the crushing device, and the lithium ion accumulator transported to the crushing device can be crushed by the crushing device; an intermediate charging container, in which the lithium ion accumulators crushed by the crushing device can be transported from the crushing device to the intermediate charging container, and the crushed lithium ion accumulators transported to the intermediate charging container can be received by the intermediate charging container; a rotary kiln, wherein the crushed lithium ion accumulators received in the intermediate charging vessel can be transported from the intermediate charging vessel into the rotary kiln, the rotary kiln can be electrically heated, and the crushed lithium ion accumulators transported into the rotary kiln can be heat treated by the rotary kiln; and a discharge conveyor device, wherein the crushed lithium ion batteries that have been heat-treated in the rotary kiln can be transported from the rotary kiln by the discharge conveyor device.

[0008] The invention is based on the basic idea of ​​providing a device for processing lithium ion accumulators, with which the latter can be processed in such a way that the raw materials present in them can be recovered after processing, while at the same time the device is designed to be mobile, so that all the components of the device are designed to be mobile as a whole, i.e. can be transported as a whole, and can interact with each other.

[0009] Because the device has such mobility or transportability, it can be transported in its entirety, for example, the device can be transported to a location where the lithium ion accumulators to be treated are collected, so that the lithium ion accumulators can be treated without being transported by the device according to the invention.

[0010] Preferably, a mobile device according to the present invention is designed to be mobile or portable in its functional configuration, ie such that the device does not have to be disassembled for transportation.

[0011] According to a preferred embodiment, the mobile device is arranged in at least one movable container, whereby the device according to the invention is made mobile by the mobility or transportability of at least one container. For example, the device can be arranged in two or more containers, which can be coupled to each other, such that, for example, when the containers are coupled to each other, the device according to the invention results.

[0012] According to a particularly preferred embodiment, the device according to the invention can be operated solely by electric current, in other words, the device according to the invention thereby only requires a supply of electric current for its functionality and does not require any further supplies, such as a supply of gas, oil or water.

[0013] Preferably, therefore, all components of the device according to the invention are designed to be operable by electric current.

[0014] In order to be able to feed the lithium ion accumulators to be treated by the device according to the invention into the device, the device according to the invention has an input chamber. The lithium ion accumulators to be treated by the device according to the invention can be received in this input chamber. In order to be able to feed the lithium ion accumulators into the input chamber, the input chamber preferably has an input opening through which the lithium ion accumulators can be fed into the input chamber. According to a preferred embodiment, an inert gas atmosphere is adjustable in the input chamber. The possibility of adjusting such an inert gas atmosphere in the input chamber has the advantage in particular that this makes it possible to prevent reactive gases from passing through the input chamber into the components of the device according to the invention which are connected downstream of the input chamber. Preferably, an inert gas atmosphere based on nitrogen can be set in the input chamber. It is preferably provided that the input chamber can be closed in an airtight manner. This prevents reactive gases from entering the input chamber when an inert gas atmosphere is set in the input chamber. Preferably, the input chamber has a gas inlet for introducing an inert gas into the input chamber. Preferably, the input chamber has an opening through which the lithium ion accumulator received in the input chamber can be conveyed into a crushing device downstream of the input chamber. Preferably, this discharge opening can be closed in an airtight manner.

[0015] The crushing device is connected downstream of the input chamber in the process direction. The lithium ion accumulators received in the input chamber can be transported from the input chamber to the crushing device. According to a preferred embodiment, the lithium ion accumulators accommodated in the input chamber can be transported from the input chamber to the crushing device by means of gravity. In particular, this also has the advantage that no separate transport unit is required to transport the lithium ion accumulators from the input chamber to the crushing device, which allows for a further compactification of the device and thus increases the mobility of the device. As mentioned above, insofar as the input chamber has a closable discharge opening, the lithium ion accumulators received in the input chamber can be transported by gravity from the input chamber to the shredding device by opening the discharge opening. According to a preferred embodiment, the crushing device is arranged below the input chamber, whereby the lithium ion accumulators can be particularly easily transported by gravity from the input chamber to the shredding device.

[0016] According to one embodiment, it is provided that the lithium ion accumulator can be crushed to a particle size by a crushing device, whereby at least 90% by weight of the lithium ion accumulator crushed by the crushing device has a particle size of at most 20 mm, particularly preferably at most 15 mm. As will be further explained below, the lithium ion accumulator can preferably be heat treated in a rotary kiln so as to be at least partially pyrolyzed. According to the invention, it has been found that if the lithium ion accumulator is crushed to a particle size of more than 20 mm or even to a particle size of only more than 15 mm, sufficient pyrolysis is not achievable or is not achievable at regular intervals. Therefore, according to the invention, it is preferably provided that the lithium ion accumulator is mainly crushed to a particle size below this critical size by a crushing device, as described above.

[0017] The particle size of the crushed lithium ion accumulator may preferably be measured using sieve analysis.

[0018] According to a preferred embodiment, the shredding device comprises a single-shaft shredder. Single-shaft shredders, also called single-shaft crushers, are known in the prior art. Single-shaft shredders generally comprise a rotatable shaft on which rotor knives are arranged in the circumferential direction. A cutting gap is formed between the shaft and an edge on which the counter knives are arranged. Due to the rotation of the shaft, the components in the cutting gap are shredded by being cut in the cutting gap between the rotor knives and the counter knives. According to the invention, it was surprisingly found that lithium-ion accumulators can be shredded particularly advantageously with such a single-shaft shredder, in particular to a particle size of up to 20 mm or up to 15 mm. Furthermore, according to the invention, it was surprisingly found that such a size reduction to a size of up to 20 mm or up to 15 mm cannot be achieved with many other size reduction units available on the market, for example biaxial shredders. This applies in particular to the shredding of the polymer film that is usually present in lithium-ion accumulators. According to a preferred embodiment, the shredding device comprises a single-shaft shredder and a punch. The punch can be used to guide the lithium-ion batteries against the cutting gap of the single-shaft shredder or the single-shaft shredder, which makes it possible to achieve an optimal comminution of the lithium-ion batteries in a particularly reliable manner, in particular to the aforementioned particle size. Preferably, the punch can be hydraulically driven.

[0019] The mobile device according to the invention has an intermediate charging vessel downstream of the crushing device in the process direction. The intermediate charging vessel is a vessel into which the lithium-ion accumulators crushed by the crushing device can be placed before being fed into the rotary kiln. The intermediate charging vessel therefore also serves as a buffer for the crushed lithium-ion accumulators, in particular between the crushing device and the rotary kiln. This effect of the intermediate charging vessel as a buffer also has the special advantage that the mobile device according to the invention can be operated continuously, even if the lithium-ion accumulators are only charged discontinuously or batchwise or are only fed into the loading chamber batchwise.

[0020] According to a preferred embodiment, it is provided that the lithium ion accumulators crushed by the crushing device can be transported from the crushing device to the intermediate charging vessel by gravity. Such transport by gravity has the advantage in particular that a separate transport device for transporting the crushed lithium ion accumulators from the crushing device to the intermediate charging vessel is not required. In particular, this also brings the advantage of adding compactness to the device according to the invention and thus improving its mobility. Preferably, the intermediate charging vessel is arranged below the crushing device, so that the crushed lithium ion accumulators can be particularly easily transported from the crushing device to the intermediate charging vessel by gravity.

[0021] It has proven to be advantageous if at least 100 liters, particularly preferably at least 150 liters, of crushed lithium-ion accumulators can be accommodated in the intermediate filling vessel.

[0022] The rotary kiln of the device according to the invention can be designed substantially like a rotary kiln of the prior art. Preferably, the rotary kiln comprises a rotary tube rotatably mounted about its longitudinal axis, the longitudinal axis being inclined relative to the horizontal. According to the invention, an inclination in the range between 0 and 3°, particularly advantageously in the range between 1 and 3°, has proven to be advantageous. A combustion chamber is formed inside the rotary kiln, in which the material to be burned can be heat-treated. By rotating the rotary kiln about its longitudinal axis, the material to be burned is automatically moved from the upper end to the lower end of the rotary kiln due to the inclination of the longitudinal axis. Thus, the material to be heat-treated in the rotary kiln is moved from the kiln inlet, which is the upper end of the rotary kiln tube, to the kiln outlet, which is the lower end of the rotary kiln tube. The material to be burned is fed into the rotary kiln at the kiln inlet and discharged from the rotary kiln at the kiln outlet.

[0023] According to a preferred embodiment, it can be provided that the rotary tube has an internal spiral, which has been found according to the invention to allow the crushed lithium-ion accumulators to be transported through the rotary kiln in a particularly advantageous manner during their heat treatment.

[0024] According to a preferred embodiment, it can be provided that the rotary kiln tube has baffles projecting into the combustion chamber. According to the invention, it has been found that the crushed lithium-ion accumulators can be mixed particularly advantageously by means of these baffles and that heat can be transferred particularly well.

[0025] In the device according to the invention, the crushed lithium-ion accumulators conveyed into the rotary kiln can preferably be heat-treated by the rotary kiln so that at least partial pyrolysis of the lithium-ion accumulators takes place. In such pyrolysis, also called pyrolysis, it is known that a thermochemical transformation takes place in which organic matter is split with substantial exclusion of oxygen. Preferably, the heat treatment in the rotary kiln is carried out in an inert gas atmosphere, which can preferably be set in the rotary kiln for that purpose. Preferably, an inert gas atmosphere based on nitrogen can be set. To set such an inert gas atmosphere, an inert gas can preferably be introduced into the rotary kiln. Preferably, the rotary kiln has a gas inlet for this purpose, through which the inert gas can be introduced into the rotary kiln. Preferably, the rotary kiln has such a gas inlet in the region of the kiln inlet, i.e. in the region where the material to be heated can be introduced into the rotary kiln.

[0026] Preferably, the rotary kiln has a gas outlet through which the combustion gases (process gases) can be discharged from the rotary kiln. In particular, the combustion gases include the inert gases present in the rotary kiln and also the pyrolysis gases formed during the thermal treatment of the lithium-ion accumulators in the rotary kiln. The combustion gases discharged from the rotary kiln can preferably be sent to a post-treatment. In particular, a thermal post-treatment of the combustion gases can be provided to render the particularly harmful components in the combustion gases harmless.

[0027] Preferably, a temperature in the range between 250°C and 650°C may be set in the rotary kiln, i.e. in the rotary tube or in the combustion chamber of the rotary kiln. According to the invention, it has been found that complete pyrolysis of the lithium-ion accumulators that may be treated in the rotary kiln is not guaranteed if the temperature is below 250°C. Furthermore, according to the invention, it has been found that undesirable partial melting of the components of the lithium-ion accumulators may occur in the rotary kiln if the temperature exceeds 650°C. Particularly preferably, the rotary kiln may be set at a temperature in the range between 500°C and 550°C. Preferably, the lithium-ion accumulators are heat treated in the rotary kiln for a duration in the range between 10 and 150 minutes.

[0028] According to a particularly preferred embodiment, the rotary kiln is an indirectly heated rotary kiln. As is known, in an indirectly heated rotary kiln, heat is generated outside the rotary kiln and transferred to the combustion chamber in the rotary kiln tube via the rotary kiln tube. According to the invention, it has been found that in a directly heated rotary kiln, in which heat is generated inside the rotary kiln, in particular by gas burners, undesirable melting of the lithium ion accumulator in the rotary kiln occurs, which can clog the rotary kiln or make the thermal treatment of the lithium ion accumulator more difficult. However, the use of an indirectly heated rotary kiln results in a particularly gentle thermal treatment of the lithium ion accumulator in the combustion chamber, which can suppress such melting reactions. Particularly preferably, an electrically indirectly heated rotary kiln is provided, in which the electrical heating is preferably performed by electrical heating elements or heating rods, particularly preferably silicon carbide heating rods, arranged preferably outside the rotary kiln. As is known from the prior art, such electrically indirectly heated rotary kilns may be equipped with an external insulating heating muffle, and heating rods or heating elements may be arranged in the space between the rotary kiln tubes and the heating muffle.

[0029] A particular advantage of such an electrically indirectly heated rotary kiln according to the invention is that it only has to be connected to a power supply in order to operate. No additional supplies, such as gas or oil, are required. In this way, in particular the object according to the invention of operating the device according to the invention only via an external power supply can also be achieved.

[0030] The rotary kiln preferably operates on a direct current principle. In this respect, the rotary kiln is preferably installed in such a way that the lithium ion batteries heat treated in the rotary kiln and the kiln gases are guided from the inlet side of the rotary kiln to the outlet side or through a combustion chamber defined by the rotary kiln.

[0031] According to a preferred embodiment, it is provided that the mobile device according to the invention further comprises an input conveyor device, by which the lithium ion accumulators accommodated in the intermediate charging vessel can be transported from the intermediate charging vessel into the rotary kiln. The input conveyor device is thus designed such that the crushed lithium ion batteries held in the intermediate charging vessel or in the buffer can be transported by the input conveyor device from the intermediate charging vessel into the rotary kiln and then heat treated there.

[0032] According to a particularly preferred embodiment, the input conveyor device comprises at least two screw conveyors. According to the invention, it has been found that the lithium ion accumulators crushed by the crushing device can be very advantageously transported by a screw conveyor and conveyed to the rotary kiln, in particular insofar as they are mainly crushed to a particle size of at most 20 mm or 15 mm, as explained before. According to a further development of the inventive idea, the input conveyor device comprises at least a first screw conveyor, which can be used when the crushed lithium ion accumulators are removed from the intermediate filling vessel, and a second screw conveyor, which can be used when the crushed lithium ion accumulators are conveyed into the rotary kiln. Preferably, the first and second screw conveyors are formed in such a way that the crushed lithium ion accumulators conveyed by the first screw conveyor can be transferred to the second screw conveyor. An input conveyor device comprising at least two such screw conveyors has a number of advantages. First of all, two such screw conveyors may be movable relative to each other, allowing the second screw conveyor to be easily adjusted to the desired inclination of the rotary kiln. In addition, however, this also allows the first and second screw conveyors to be made of different materials. For example, the second screw conveyor may be made of high-strength steel that can withstand the harsh conditions of the inlet of the rotary kiln so that the second screw conveyor can transport the lithium-ion batteries crushed there into the rotary kiln. However, the first screw conveyor may be made of a more preferable material, in particular a more preferable steel, that does not have to withstand such harsh conditions.

[0033] According to a preferred embodiment, it is provided that the rotary kiln comprises a rotary tube and an inlet housing, the rotary tube being sealed with respect to the inlet housing via a seal comprising a polytetrafluoroethylene or carbon ring seal. As known from the prior art, the inlet housing is preferably arranged in the region of the furnace inlet. Corresponding inlet housings are known from the prior art. They serve to receive the material to be heat-treated in the rotary kiln before being introduced into the rotary kiln. According to the invention, the crushed lithium-ion accumulators can be preferably conveyed into the inlet housing by a feed conveyor device, particularly preferably by a second screw conveyor. The crushed lithium-ion accumulators conveyed into the inlet housing can then be conveyed into the rotary kiln and heat-treated there.

[0034] According to a preferred embodiment, it may be provided that the rotary kiln comprises a cooling device in the region of the inlet housing. Such a cooling device may be designed in particular in such a way that the rotary kiln can be cooled in the region of its inlet housing. Preferably, the cooling device is designed in such a way that the rotary kiln can be cooled with a gas, in particular with air, in the region of its inlet housing. It is particularly preferred that the cooling device is designed in such a way that the rotary kiln can be cooled with a gas from the outside. Such a cooling device may in particular prevent polytetrafluoroethylene from pyrolyzing at higher temperatures.

[0035] According to one preferred embodiment, it is provided that the rotary kiln comprises a rotary tube and an outlet housing, the rotary tube being sealed with respect to the outlet housing via a seal comprising a polytetrafluoroethylene or carbon ring seal.

[0036] As known from the prior art, the outlet housing is preferably arranged in the region of the furnace outlet. Corresponding outlet housings are known from the prior art. They are used to accommodate the material heat-treated in the rotary kiln after it has been discharged from the rotary kiln. In this process, the material heat-treated in the rotary kiln is periodically fed into the outlet housing by the rotation of the rotary kiln. A technical problem with rotary kilns of the prior art is the sealing of the rotary kiln tubes to the outlet housing, since the outlet housing is regularly arranged in a fixed position, whereas the rotary kiln tubes are rotatably guided in the outlet housing. According to the invention, it has now surprisingly been found that the rotary kiln of the mobile device according to the invention can be very advantageously sealed with respect to the outlet housing using a seal comprising polytetrafluoroethylene.

[0037] As explained before, the inert gas atmosphere is preferably adjustable in the rotary kiln. According to a further development of the inventive concept, an inert gas atmosphere can preferably also be set in the components of the device that are downstream of the feed chamber in the process direction. This can prevent reaction gases from these components from entering the rotary kiln, which could disturb the pyrolysis of the lithium-ion batteries.

[0038] The discharge conveyor device of the mobile device according to the invention can essentially be any conveyor known from the prior art, by means of which the material treated in the rotary kiln can be conveyed out of the rotary kiln. According to a preferred embodiment, the discharge conveyor device comprises a rotary valve. Preferably, the lithium-ion batteries heat-treated in the rotary kiln can be conveyed, if necessary, into the discharge conveyor device or into a cellular wheel-type sluice of the discharge conveyor device via the outlet housing formed as described above. Preferably, the lithium-ion batteries can be conveyed by gravity into the discharge conveyor device, in particular into the rotary valve of the discharge conveyor device. This makes additional conveying devices unnecessary and increases the mobility of the device according to the invention.

[0039] According to a particularly preferred embodiment, the mobile device according to the invention further comprises an intermediate outlet container, in which the lithium ion batteries discharged from the rotary kiln by means of the discharge conveyor device can be accommodated. The intermediate outlet container is in this respect a buffer in which the heat-treated lithium ion batteries discharged from the rotary kiln by the discharge conveyor device can be received before being further processed or transported. This then allows the rotary kiln to be operated continuously, while the heat-treated lithium ion batteries discharged from the rotary kiln can be further processed or transported only discontinuously, i.e. in batches.

[0040] According to one embodiment, it may be provided that the mobile device according to the invention comprises a screw conveyor through which the lithium ion accumulators contained in the intermediate discharge container can be discharged. The screw conveyor can then transport the lithium ion accumulators to any receiving device. According to a preferred embodiment, it is provided that the screw conveyor is preferably cooled with a fluid, for example in the form of water or oil. It is preferably provided that the fluid is circulated and not consumed. The heat is preferably dissipated to the environment.

[0041] According to a preferred embodiment, it may be provided that the mobile device according to the invention comprises a device for generating inert gas. In particular, the device according to the invention may comprise such a device for generating gaseous nitrogen. A particular advantage of such a device for generating inert gas is, in particular, that the device according to the invention does not have to be connected to an external inert gas source for its operation. Rather, the presence of such a device allows the device according to the invention to be operated only by connection to an external power supply. The device for generating inert gas, in particular gaseous nitrogen, can in principle be any device known from the prior art for generating inert gas, in particular gaseous nitrogen. Particularly preferably, such a device is a device that can be operated only with connection to an external power supply. Preferably, the device is a nitrogen generator, particularly preferably a nitrogen generator based on the pressure swing principle with a carbon molecular sieve. Preferably, the nitrogen generator is fed by a screw air compressor.

[0042] According to a further embodiment of the invention it may be provided that the device further comprises a tank for storing the inert gas produced by the device for generating inert gas.

[0043] Moreover, according to a further development of the inventive idea, it can be provided that the device comprises means for conducting the inert gas from a tank into the rotary kiln, in particular into the rotary tube of the rotary kiln, in particular in the region of the kiln inlet. Furthermore, means can be provided for introducing the inert gas from a tank into the loading chamber.

[0044] Preferably, the mobile device according to the invention comprises control means making it possible to control the device. Preferably, these control means comprise an electronic data processing device, by means of which the device can be controlled. In particular, the control means can be used to control or monitor the operation of all the components of the device. In particular, the operation of the rotary kiln, i.e. in particular the temperature and the atmosphere of the rotary kiln, can be or are controlled by the control means.

[0045] It is also an object of the present invention to provide a method for treating a lithium-ion accumulator, comprising the steps of: Providing a mobile device according to the present invention; Loading a lithium ion accumulator into a loading chamber; transporting the lithium ion accumulator fed into the input chamber to a crushing device; Crushing the lithium ion accumulator by a crushing device; conveying the crushed lithium ion accumulators to an intermediate filling vessel; Transporting the crushed lithium ion accumulators transported in the intermediate filling vessel into a rotary kiln; A step of heat treating the crushed lithium ion accumulators transported into the rotary kiln by the rotary kiln; and transporting the crushed lithium ion accumulators that have been heat-treated in the rotary kiln from the rotary kiln by a discharge conveyor device.

[0046] The method according to the invention is preferably carried out in such a way that the lithium-ion accumulator is treated as described above.

[0047] In this regard, the lithium ion accumulator is preferably heat treated in a rotary kiln to cause at least partial pyrolysis of the lithium ion accumulator, as previously described.

[0048] Lithium-ion accumulators that have been thermally treated by means of the mobile device according to the invention, in particular by means of the method according to the invention, can then be further processed so that the aforementioned raw materials can be at least partially recovered from them.

[0049] Further features of the present invention will be apparent from the claims, the figures, and the following description of the accompanying figures.

[0050] All the features of the invention may be combined with one another in any desired manner, either individually or in combination.

[0051] An example of one embodiment of the present invention will now be described in more detail with reference to the accompanying highly schematic drawings and the associated following figure description.

[0052] The figure is explained below. [Brief description of the drawings]

[0053] [Figure 1] FIG. 1 is a schematic process diagram of one embodiment of the apparatus according to the invention and the method according to the invention. [Diagram 2] FIG. 2 is a side view of an embodiment of the device according to FIG. 1; DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0054] Generally, the mobile device of FIG.

[0055] The device 1 comprises an input chamber 10 into which the lithium-ion battery 11 can be inserted according to the arrow P1 via an input opening 12. The input opening 12 can be closed in an airtight manner via a first flap 13. At the bottom, the input chamber 10 has a discharge opening 14 which can be closed in an airtight manner via a second flap 15. The input chamber 10 has a volume of 250 liters and can be closed in an airtight manner by the first flap 13 and the second flap 15. The input chamber 10 has a gas connection 16 for introducing an inert gas into the input chamber 10. By introducing an inert gas by means of the gas connection 16, an inert gas atmosphere can be set in the input chamber 10.

[0056] The crushing device 20 of the device 1 is arranged below the input chamber 10. By arranging the crushing device 20 below the input chamber 10, the lithium-ion accumulators can be transported by gravity from the input chamber 10 to the crushing device 20. By opening the second flap 15 of the input chamber 10, the lithium-ion accumulators arranged in the input chamber 10 fall into the crushing device 20 by gravity. The crushing device 20 is a single-shaft shredder, and the material to be shredded is pressed against the shaft of the single-shaft shredder by means of a hydraulic ram. The single-shaft shredder can shred the lithium-ion batteries almost completely to the extent that more than 90% by mass of the lithium-ion accumulators are present with a particle size of 15 mm or less. The transport path of the lithium-ion accumulators from the input chamber 10 to the crushing device 20 is indicated by the arrow P2. The lithium-ion accumulators shredded in the crushing device 20 are indicated by black circles 21.

[0057] The intermediate charging vessel 30 is arranged below the crusher 20. The intermediate charging vessel 30 is designed as a simple steel box and serves as a buffer between the input chamber 10, which is upstream in the process direction, the crusher 20 and the rotary kiln 50, which is downstream in the process direction. Arranging the intermediate charging vessel 30 below the crusher 20 allows the lithium-ion accumulators crushed in the crusher 20 to fall by gravity from the crusher 20 into the intermediate charging vessel 30, which is indicated by the arrow P3. The intermediate charging vessel 30 has a volume of about 150 liters.

[0058] The mobile device 1 further comprises a rotary kiln 50 and an input conveyor device 40, via which the crushed lithium ion accumulators received in the intermediate charging vessel 30 can be transported from the intermediate charging vessel 30 into the rotary kiln 50.

[0059] The rotary kiln 50 is in the form of a rotary kiln 50 that can be indirectly heated electrically via silicon carbide heating rods. The rotary kiln 50 comprises a cylindrical rotary tube 51 that is rotatably mounted about a central longitudinal axis L of the rotary tube 51. The central longitudinal axis L is inclined relative to the horizontal. The rotary tube 51 is made of stainless, austenitic chromium-nickel-molybdenum steel with a low carbon content. The upper end of the rotary kiln 51, on the left side of FIG. 1, is the kiln inlet section 52 of the rotary kiln 50, through which the crushed lithium ion batteries to be heat-treated in the rotary kiln 50 can be fed into the rotary kiln 51. The lower end of the rotary kiln 51, on the right side of FIG. 1, is the kiln outlet section 53 of the rotary kiln 51, through which the lithium ion batteries heat-treated in the rotary kiln 50 are discharged from the rotary kiln 51. The rotary kiln 51 is insulated from the outside by a heating muffle (not shown) and silicon carbide fuel rods (not shown) are arranged between the rotary kiln 51 and the heating muffle. Electrical heating of the rotary kiln 51 via silicon carbide heating rods is carried out according to the prior art. In this respect, the rotary tube 51 is heated from the outside via the heating rods, so that heat is conducted through the rotary tube 51 into the space enclosed by the rotary tube 51. The space enclosed by the rotary kiln tube 51 thus serves as a combustion chamber in which the crushed lithium-ion batteries can be thermally treated. The control device controls the rotary kiln 50 so that the temperature throughout the rotary kiln 51 is in the range of 500 to 550 ° C. In the region of the inlet section 52, the rotary kiln 50 has an inlet housing 54 into which the rotary kiln 51 is partially introduced and with respect to which the rotary kiln 51 is sealed by a seal 55 comprising polytetrafluoroethylene. Similarly, in the region of the outlet section 53, the rotary kiln 50 comprises an outlet housing 56 into which the rotary tube 51 is also partially inserted and to which the rotary tube 51 is sealed by a seal 57 comprising polytetrafluoroethylene.The device 1 further comprises an air cooler 60, by means of which the rotary kiln 50 can be cooled in the region of the inlet section 52 and the outlet section 53 of the rotary tube 51. For this purpose, the cooler 60 comprises a fan 61, by means of which the rotary kiln 51 is cooled from the outside in the region of the inlet section 52 via a first cooling line 62, and the rotary kiln 51 can be cooled from the outside in the region of the outlet section 53 via a second line 63 by blowing in air (fresh air). This allows the rotary tube 51 to be cooled so that the seals 55, 57, which comprise polytetrafluoroethylene, can be protected from thermal damage.

[0060] The input conveyor device 40 comprises a first screw conveyor 41 and a second screw conveyor 42. By using the first screw conveyor 41, the crushed lithium ion accumulators 21 arranged in the intermediate charging vessel 30 can be conveyed out of the intermediate charging vessel 30. At the transfer point 43, the first screw conveyor 41 transfers the crushed lithium ion accumulators 21 to the second screw conveyor 42, via which the crushed lithium ion accumulators 21 can finally be conveyed into the inlet housing 54 of the rotary kiln 50. The conveyance of the crushed lithium ion accumulators 21 by the first screw conveyor 41 and the second screw conveyor 42 is indicated by the arrow P4, and the entry of the crushed lithium ion accumulators 21 from the second screw conveyor 42 into the inlet housing 54 is indicated by the arrow P5.

[0061] By rotating the rotary tube 51 about the central longitudinal axis L, the crushed lithium ion accumulators 21 are transported from the inlet housing 54 into the rotary tube 51 and through it to the outlet housing 56 along the direction of the arrow P6. During its passage through the rotary tube 51, the crushed lithium ion accumulators 21 are heat treated so as to be pyrolyzed. To supply the inert gas atmosphere required for such pyrolysis into the rotary kiln 51, the rotary kiln 51 has a gas supply 58 in the region of the inlet 52, through which the inert gas can be introduced into the rotary kiln 51. The inert gas introduced into the rotary kiln 51 flows in the rotary kiln 51 in the direction of the arrow P6 and, on reaching the region of the outlet 53, the fuel gas indicated by the arrow 59 is again withdrawn from the rotary kiln 50. The withdrawn fuel gas can then be post-treated by a fuel gas post-treatment process not shown in the figure.

[0062] In the area of ​​the outlet 53, the lithium-ion accumulators 21 pyrolyzed in the rotary kiln 51 fall by gravity into the outlet housing 56, indicated by the arrow P7, from where they then fall by gravity into a discharge conveyor device 70 in the form of a rotary valve. Below the rotary valve 70, an intermediate outlet container 80 in the form of a simple steel box is arranged as a buffer. The intermediate outlet container 80 is arranged below the rotary valve 70 so that the heat-treated lithium-ion cells 21 can fall by gravity from the rotary valve 70 into the intermediate outlet container 80, indicated by the arrow P9. Finally, the lithium-ion accumulators 21 can be discharged from the intermediate outlet container 80 along the direction of the arrow P10 and conveyed via a further conveying screw 90 into a conveying container 100, indicated by the arrow P11. The screw conveyor 90 has a water-supply jacket cooling system so that the lithium-ion accumulators 21 can be cooled down to a maximum temperature of 60° C. while being conveyed through the screw conveyor 90.

[0063] Via the transport container 100, the crushed heat-treated lithium-ion accumulators 21 can be removed in bulk from the device 1 and sent for further processing. This bulk removal is buffered by an intermediate outlet container 80.

[0064] The mobile device 1 further comprises means 110 for generating an inert gas in the form of gaseous nitrogen. The means 110 comprises an air screw compressor 111 that can be used to generate gaseous nitrogen. Furthermore, the means 110 comprises a gas tank 112 in which the nitrogen gas generated by the air screw compressor 111 can be received. From the gas tank 112, the nitrogen can be introduced into the input chamber 10 via the gas opening 16 using a first inert gas line 113 on the one hand, and into the rotary tube 51 via the gas connection 58 using a second inert gas line 114 on the other hand.

[0065] All components of the device 1 may be current driven, so only a supply of current is required to operate the device 1.

[0066] Moreover, the device 1 as a whole is designed to be completely disposed within a container, which is indicated by dashed line 120. By transporting the container 120, the entire device 1 is designed to be fully transportable or mobile.

[0067] In FIG. 2, only some elements of the device 1 according to FIG. 1 are marked with reference symbols. [Explanation of symbols]

[0068] 1 device 10 Input chamber 11 Lithium-ion battery 12 Input opening 13 First flap 14 Discharge opening 15 Second flap 16 Gas connection 20 Crushing Equipment 30 Intermediate filling container 40 Input conveyor device 41 First Screw Conveyor 42 Second Screw Conveyor 43 Transfer Point 50 Rotary Kiln 51 Cylindrical Rotary Tube 52 Kiln entrance 53 Kiln outlet 54 Inlet housing 55 Seal 56 Outlet housing 57 Seal 58 Gas Supply Section 60 Cooler 61 Fans 62 First cooling line 63 Second Pipeline 70 Discharge conveyor device 80 Intermediate outlet container 90 Conveying screw 100 Transport container 110 means 111 Air screw compressor 112 Gas Tank 113 First inert gas line 114 Second inert gas line

Claims

1. A mobile device (1) for processing lithium-ion accumulators, comprising: 1.1 An input chamber (10), 1.1.1 A lithium ion accumulator is receivable within said input chamber (10); An input chamber (10); 1.2 A crushing device (20), 1.2.1 the lithium ion accumulator received in the input chamber (10) is transportable from the input chamber (10) to the crushing device (20); 1.2.2 The lithium ion accumulator transported to the crushing device (20) can be crushed by the crushing device (20); A crushing device (20); 1.3 An intermediate filling container (30), 1.3.1 The lithium ion accumulator crushed by the crushing device (20) can be transported from the crushing device (20) to an intermediate filling container (30); 1.3.2 The crushed lithium ion accumulators delivered to the intermediate charging vessel (30) are acceptable to said intermediate charging vessel (30); An intermediate filling container (30); 1.4 A rotary kiln (50), 1.4.1 The crushed lithium ion accumulators received in the intermediate charging vessel (30) are transportable from the intermediate charging vessel (30) into the rotary kiln (50); 1.4.2 The rotary kiln (50) is electrically heatable; 1.4.3 The crushed lithium ion accumulators transported into the rotary kiln (50) can be heat treated by the rotary kiln (50); A rotary kiln (50); 1.5 A discharge conveyor device (70) comprising: 1.5.1 The crushed lithium ion accumulators heat-treated in the rotary kiln (50) can be discharged from the rotary kiln (50) by the discharge conveyor device (70); A discharge conveyor device (70) and A mobile device (1).

2. A mobile device (1) as described in claim 1, wherein an inert gas atmosphere can be set in the loading chamber (10).

3. 3. The mobile device (1) according to at least one of claims 1 to 2, wherein the lithium ion accumulator housed in the input chamber (10) can be transported from the input chamber (10) to the crushing device (20) using gravity.

4. The lithium ion accumulators may be crushed by the crushing device (20) to a particle size such that at least 90% by mass of the lithium ion accumulators crushed by the crushing device (20) have a particle size of at most 20 mm.

5. The mobile device (1) according to at least one of claims 1 to 4, wherein the crushing device (20) comprises a single-shaft shredder.

6. 6. The mobile device (1) according to at least one of claims 1 to 5, wherein the lithium ion accumulators crushed by the crushing device (20) can be transported from the crushing device (20) to the intermediate filling vessel (30) using gravity.

7. 7. The mobile device (1) according to at least one of claims 1 to 6, wherein the crushed lithium ion accumulators transported into the rotary kiln (50) can be thermally treated by the rotary kiln (50) so as to cause at least partial pyrolysis of the lithium ion accumulators.

8. 8. The mobile device (1) according to at least one of claims 1 to 7, further comprising an input conveyor device (40), wherein the lithium ion accumulators contained in the intermediate filling vessel (30) can be transported from the intermediate filling vessel (30) into the rotary kiln (50) by the input conveyor device (40).

9. 9. The mobile device (1) according to claim 8, wherein the input conveyor device (40) comprises at least two screw conveyors (41, 42).

10. 10. The mobile device (1) according to at least one of claims 1 to 9, wherein the rotary kiln (50) comprises a rotary tube (51) and an inlet housing (54), the rotary tube (51) being sealed with respect to the inlet housing (54) via a seal (55) comprising polytetrafluoroethylene.

11. 11. The mobile device (1) according to at least one of claims 1 to 10, wherein the rotary kiln (50) comprises a rotary tube (51) and an outlet housing (56), the rotary tube (51) being sealed with respect to the outlet housing (56) via a seal (57) comprising polytetrafluoroethylene.

12. 12. The mobile device (1) according to at least one of claims 1 to 11, further comprising an intermediate outlet container (80), wherein the lithium ion accumulators transported from the rotary kiln (50) by means of the discharge conveyor device (70) can be accommodated in the intermediate outlet container (80).

13. A mobile device (1) as described in at least one of claims 1 to 12, further comprising means (110) for generating an inert gas.

14. 1. A method of treating a lithium ion accumulator, comprising: A. Providing a mobile device (1) according to at least one of claims 1 to 13; B. Loading a lithium ion accumulator (11) into the loading chamber (10); C. Transporting the lithium ion accumulator (11) loaded into the loading chamber (10) to the crushing device (20); D. Crushing the lithium ion accumulator (11) by the crushing device (20); E. Transporting the crushed lithium ion accumulators (21) to an intermediate charging vessel (30); F. The crushed lithium ion accumulator (21) transported in the intermediate charging vessel (30) is transported into the rotary kiln (50); G. Heat treating the crushed lithium ion accumulators (21) transported into the rotary kiln (50) by the rotary kiln (50); H. A step of discharging the crushed lithium ion accumulators (21) that have been heat-treated in the rotary kiln (50) from the rotary kiln (50) by the discharge conveyor device (70); A method comprising:

15. 15. The method according to claim 14, wherein the lithium ion accumulators (11) are thermally treated by the rotary kiln (50) to cause at least partial pyrolysis of the crushed lithium ion accumulators (21).

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