WO2023029636A1 - Lithium chip inerting processing apparartus and processing method, and battery lithium supplementing system - Google Patents

Lithium chip inerting processing apparartus and processing method, and battery lithium supplementing system Download PDF

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Publication number
WO2023029636A1
WO2023029636A1 PCT/CN2022/097791 CN2022097791W WO2023029636A1 WO 2023029636 A1 WO2023029636 A1 WO 2023029636A1 CN 2022097791 W CN2022097791 W CN 2022097791W WO 2023029636 A1 WO2023029636 A1 WO 2023029636A1
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Prior art keywords
lithium
pipeline
gas
treatment device
infiltration
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PCT/CN2022/097791
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French (fr)
Chinese (zh)
Inventor
费新路
李克强
赵丰刚
卢毅
谢斌
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宁德时代新能源科技股份有限公司
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Publication of WO2023029636A1 publication Critical patent/WO2023029636A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/16Metallic particles coated with a non-metal
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1391Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • 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

Definitions

  • the present application relates to the technical field of battery production, in particular to a lithium scrap inerting treatment device and treatment method, and a battery lithium replenishment system.
  • Lithium-ion battery cells are widely used in electronic equipment, such as mobile phones, laptop computers, battery cars, electric vehicles, electric aircraft, electric ships, electric toy cars, electric toy ships, electric toy planes and electric tools, etc.
  • lithium shavings may be produced, and lithium shavings are likely to cause safety problems. How to enhance the safety of battery cell production is an urgent technical problem in battery technology.
  • the present application provides a lithium scrap inerting treatment device and treatment method, and a battery lithium replenishment system, aiming at improving the safety of battery production.
  • an embodiment of the present application provides a device for inerting lithium scraps, including: a first pipeline, including an inlet end, an outlet end, and an infiltration chamber between the inlet end and the outlet end, and the outlet end is used for Connected with an external drainage system, the drainage system is used to drive the gas containing lithium chips to flow through the first pipeline, the infiltration chamber is used to accommodate the infiltration liquid, so as to infiltrate the lithium chips when the gas flows through the infiltration chamber; and the first blocking mechanism is set It is in the wetting chamber, and is used to block at least part of the wetting liquid from flowing out from the gas outlet when the gas flows through the first pipeline.
  • the gas flows from the inlet end of the first pipeline to the gas outlet end.
  • the gas can drive the immersion liquid and lithium chips to flow.
  • the first blocking mechanism can block part of the wetting liquid, so that the wetting liquid is blocked from flowing back, thereby reducing the possibility of the wetting liquid flowing out of the gas outlet together with the gas.
  • the inlet end is located above the gas outlet end in the vertical direction
  • the first blocking mechanism includes a plurality of blocking plates arranged at intervals, gaps for gas flow are formed between adjacent blocking plates, and at least Parts are inclined relative to the vertical.
  • the gas in the embodiment of the present application flows through the barrier plate of the first barrier mechanism, it flows out through the gap, and the gas drives the immersion liquid to flow together.
  • the inclined part of the barrier plate can change the flow direction of the gas to block the immersion liquid and make the immersion liquid flow back, and then Reduce the possibility of wetting liquid flowing out of the gas outlet with the gas.
  • the barrier plate includes a plurality of barrier parts, the multiple barrier parts are connected in sequence, and there is an included angle between two connected barrier parts.
  • the multiple blocking parts can change the flow direction of the gas multiple times, so that the infiltration liquid driven by the gas is blocked by the multiple blocking parts, which can further reduce the outflow of gas with the gas. terminal immersion fluid.
  • the projections of adjacent barrier panels along the vertical direction are connected.
  • the gas in the embodiment of the present application flows through the gap, the gas in the gap as a whole will be blocked by the barrier plates on both sides of the gap and change the flow direction, so as to further reduce the wetting liquid flowing out of the gas outlet with the gas.
  • a second blocking mechanism is also provided in the infiltration chamber, the second blocking mechanism is connected to the pipe wall of the first pipeline, and is located between the first blocking mechanism and the inlet end, and the second blocking mechanism is used to block Lithium chips flow out from the gas outlet. After the lithium chips are inerted by the immersion liquid, some lithium chips may continue to flow with the gas, but the second barrier mechanism in the embodiment of the present application can block the lithium chips and reduce the flow of lithium chips through the gas outlet. .
  • the cross-sectional area of the second blocking mechanism on the horizontal plane gradually increases or decreases along the vertical direction.
  • the density of lithium chips is smaller than that of the immersion liquid.
  • Lithium chips have a tendency to float up due to the buoyancy of the immersion liquid.
  • Lithium chips accumulate in the relatively high vertical part of the second barrier mechanism.
  • the swarf basically does not block the relatively lower part of the second barrier mechanism, and the gas can drive the immersion liquid to flow out from the relatively lower part of the second barrier mechanism.
  • the second blocking mechanism includes: two first plates disposed opposite to each other along the first direction, the distance between the two first plates gradually increases upward along the vertical direction; and two first plates disposed opposite to each other along the second direction
  • the two second plates, the two first plates and the two second plates are connected and enclosed to form a cavity, the first plate and/or the second plate are provided with a plurality of through holes to allow the gas and immersion liquid to flow out, Both the first direction and the second direction are parallel to the horizontal plane, and the first direction and the second direction are perpendicular.
  • the through hole can play the role of filtering lithium chips.
  • the lithium chips are mainly accumulated on the outside of the relatively higher part of the first plate in the vertical direction, and the relatively small parts of the first plate and the second plate The lower part will not be blocked by lithium shavings, and the gas can drive the immersion liquid to flow out through the first plate and/or the second plate.
  • a filter mechanism is also provided in the infiltration chamber, and the filter mechanism is located between the first blocking mechanism and the gas outlet, and is used to filter lithium debris and immersion liquid in the gas. After the gas in the embodiment of the present application flows through the first barrier mechanism, it may still carry part of the lithium debris and the wetting liquid, and the filtering function of the filtering mechanism can further reduce the lithium debris and the wetting fluid flowing out of the gas outlet.
  • the lithium scrap inerting treatment device also includes: a second pipeline, the second pipeline is connected to the first pipeline, the second pipeline includes a liquid inlet and a liquid outlet, and the liquid inlet is connected to the infiltration chamber; and the collection The collection mechanism is connected to the pipe wall of the second pipeline, and the collection mechanism is used to separate the immersion liquid and lithium chips.
  • the infiltration solution containing lithium chips is drained into the collection mechanism of the second pipeline, and the infiltration solution and lithium chips are filtered Separation, the lithium scraps are retained in the collection mechanism to achieve the purpose of collecting lithium scraps.
  • the second conduit is located vertically below the first conduit.
  • the embodiment of the present application uses the gravity of the immersion liquid and lithium chips to allow the immersion liquid and lithium chips to flow from the first pipeline to the second pipeline without additional drainage equipment, which can simplify the structure of the device.
  • the collection mechanism includes a collection chamber and a first filter, and the first filter is disposed in the collection chamber and used to separate the immersion liquid and lithium debris.
  • a first switch is further arranged in the second pipeline, the first switch is located between the collection mechanism and the liquid inlet, and the first switch is configured to control the connection between the collection mechanism and the infiltration chamber.
  • the production rhythm of the first pipeline and the second pipeline can be adjusted by using the first switch.
  • the collection mechanism is detachably disposed in the second conduit.
  • the collection mechanism in the embodiment of the present application and the second pipeline can be connected in a detachable manner, which is convenient for removing lithium chips and replacing the collection mechanism.
  • the lithium scrap inerting treatment device further includes a third pipeline
  • the third pipeline includes a first end and a second end, the first end is connected to the liquid outlet of the second pipeline, and the second end is connected to the infiltration chamber , the third pipeline is used to transport the infiltration fluid separated by the collection mechanism to the infiltration chamber.
  • the third pipeline circulates the purified infiltration fluid to the infiltration cavity, thereby improving the utilization rate of the infiltration fluid.
  • the second end is located between the outlet end and the first barrier mechanism.
  • the lithium chips adhering to the first barrier mechanism can be impacted into the immersion liquid to prevent the lithium chips from blocking the first barrier mechanism, so that the gas can Discharge smoothly.
  • an embodiment of the present application provides a battery lithium replenishment system, including: a lithium replenishment device; It is set opposite to the lithium supplementation device.
  • the lithium replenishing device is used to replenish lithium to the pole piece of the battery.
  • lithium scraps may be generated;
  • the lithium chips are pumped into the infiltration chamber, the lithium chips are infiltrated in the infiltration solution, and the surface of the lithium chips is wrapped and inerted by the infiltration solution, which can prevent spontaneous combustion of the lithium chips.
  • an embodiment of the present application provides a lithium scrap inerting treatment method, including: providing a first pipeline and a first barrier mechanism, the first pipeline includes an inlet end, an outlet end, and a gas outlet located between the inlet end and the outlet end.
  • the infiltration chamber contains the infiltration liquid
  • the first barrier mechanism is set in the infiltration chamber;
  • the drainage system is connected to the gas outlet, and the drainage system is used to drive the gas containing lithium chips to flow through the first pipeline, and the gas flows through the Lithium shavings are infiltrated when the cavity is infiltrated, wherein, when the gas flows through the first pipeline, the first blocking mechanism blocks at least part of the infiltrating liquid from flowing out from the gas outlet.
  • Figure 1 is a schematic structural view of a lithium scrap inerting treatment device provided in some embodiments of the present application.
  • Fig. 2 is a schematic structural view of the first barrier mechanism of the lithium scrap inerting treatment device provided by some embodiments of the present application;
  • Fig. 3 is a structural schematic view of the first blocking mechanism shown in Fig. 2 at another angle;
  • Fig. 4 is a structural schematic view of the first blocking mechanism shown in Fig. 2 at another angle;
  • Fig. 5 is a schematic structural view of a lithium scrap inerting treatment device provided in other embodiments of the present application.
  • Fig. 6 is a schematic structural view of the second barrier mechanism of the lithium scrap inerting treatment device provided in some embodiments of the present application.
  • Fig. 7 is a structural schematic diagram of the second blocking mechanism shown in Fig. 6 at another angle;
  • Fig. 8 is a schematic structural diagram of a lithium scrap inerting treatment device provided in some other embodiments of the present application.
  • Fig. 9 is a schematic structural view of the second filter element of the lithium scrap inerting treatment device provided in some embodiments of the present application.
  • Fig. 10 is a schematic structural view of the third filter element of the lithium scrap inerting treatment device provided in some embodiments of the present application.
  • Fig. 11 is a schematic structural view of the third filter shown in Fig. 10 at another angle;
  • Fig. 12 is a schematic structural diagram of a lithium scrap inerting treatment device provided in some further embodiments of the present application.
  • Fig. 13 is a schematic flow diagram of a lithium scrap inerting treatment method provided in some embodiments of the present application.
  • Fig. 14 is a schematic structural diagram of a lithium scrap inerting treatment device in a working state provided by some embodiments of the present application;
  • Fig. 15 is a schematic structural diagram of a lithium scrap inerting treatment device in another working state provided by some embodiments of the present application.
  • Fig. 16 is a schematic structural diagram of a lithium scrap inerting treatment device in another working state provided by some embodiments of the present application.
  • Fig. 17 is a schematic structural diagram of a lithium scrap inerting treatment device in another working state provided by some embodiments of the present application.
  • Fig. 18 is a schematic structural diagram of a battery lithium replenishment system provided by some embodiments of the present application.
  • X vertical direction
  • Y first direction
  • Z second direction
  • Lithium shavings inerting treatment device 2. Lithium replenishment device; J, immersion solution; Li, lithium shavings;
  • the first blocking mechanism 111, the blocking plate; 111a, the blocking part; 111b, the gap; 112, the connecting plate; 112a, the first side; 112b, the second side;
  • the second blocking mechanism 121, the first plate; 122, the second plate; 12a, the cavity; 12b, the through hole;
  • Filter mechanism 131, second filter element; 131a, first filter hole; 132, third filter element; 132a, second filter hole;
  • Second pipeline 20a, liquid inlet; 20b, liquid outlet; 21, collection mechanism; 211, collection chamber; 212, first filter; 22, first switch;
  • connection should be interpreted in a broad sense, for example, it can be a fixed connection or a flexible connection. Disassembled connection, or integral connection; it can be directly connected or indirectly connected through an intermediary.
  • connection should be interpreted in a broad sense, for example, it can be a fixed connection or a flexible connection. Disassembled connection, or integral connection; it can be directly connected or indirectly connected through an intermediary.
  • the battery cells may include lithium-ion secondary battery cells, lithium-ion primary battery cells, lithium-sulfur battery cells, or sodium-lithium-ion battery cells, which are not limited in the embodiments of the present application.
  • the battery cell includes an electrode assembly and an electrolyte, and the electrode assembly is composed of a pole piece and a separator assembly.
  • the pole pieces include positive pole pieces and negative pole pieces.
  • a battery cell primarily relies on the movement of metal ions, such as lithium ions, between the positive and negative plates.
  • the positive electrode sheet includes a positive electrode current collector and a positive electrode active material layer, the positive electrode active material layer is coated on the surface of the positive electrode current collector, and the positive electrode current collector that is not coated with the positive electrode active material layer protrudes from the positive electrode collector that has been coated with the positive electrode active material layer , the positive electrode current collector not coated with the positive electrode active material layer is used as the positive electrode tab.
  • the material of the positive electrode current collector can be aluminum, and the positive electrode active material can be lithium cobaltate, lithium iron phosphate, ternary lithium or lithium manganate.
  • the negative electrode sheet includes a negative electrode current collector and a negative electrode active material layer, the negative electrode active material layer is coated on the surface of the negative electrode current collector, and the negative electrode current collector that is not coated with the negative electrode active material layer protrudes from the negative electrode collector that has been coated with the negative electrode active material layer , the negative electrode current collector not coated with the negative electrode active material layer is used as the negative electrode tab.
  • the material of the negative electrode current collector may be copper, and the negative electrode active material may be carbon or silicon.
  • a solid electrolyte film solid electrolyte interphase, SEI film
  • SEI film solid electrolyte interphase, SEI film
  • the formation of the SEI film will consume part of the lithium, which will cause the loss of lithium, thereby reducing the discharge capacity of the battery cell.
  • the first charge and discharge rate is reduced.
  • a lithium replenishing device is usually used to replenish active lithium on the surface of the pole piece during the forming process of the pole piece, and the pole piece after lithium supplementation is applied to the battery cell. In this way, the discharge capacity and initial charge-discharge rate of the battery cell can be improved.
  • the lithium replenishment process of the pole piece mainly includes the calendering process and the lamination process.
  • the calendering process is to thin the lithium strip by rolling to form a lithium film
  • the lamination process is to laminate the lithium film to the surface of the pole piece by rolling.
  • lithium scraps are generated during the lithium supplementation process, and lithium scraps need to be collected and processed. Due to the relatively active chemical properties of lithium, problems such as spontaneous combustion of lithium scraps usually occur during the process of collecting and processing lithium scraps, causing safety risks.
  • the lithium scrap inerting treatment device can be used to collect and process lithium scrap produced in the process of lithium supplementation, and can ensure the safety of the process of collecting and processing lithium scrap.
  • the lithium scrap inerting treatment device can also be used to collect and process lithium scrap produced in other production processes.
  • a lithium scrap inerting treatment device provided by an embodiment of the present application includes a first pipeline 10, including an inlet end 10a, an outlet end 10b, and an infiltration chamber between the inlet end 10a and the outlet end 10b.
  • the gas outlet 10b is used to connect with the external drainage system
  • the drainage system is used to drive the gas containing lithium chips Li to flow through the first pipeline 10
  • the infiltration chamber 10c is used to accommodate the infiltration liquid J, so that when the gas flows through the infiltration chamber 10c When infiltrating lithium chips Li.
  • the first blocking mechanism 11 is arranged in the infiltration chamber 10c, and is used for blocking at least part of the infiltration liquid J from flowing out from the gas outlet end 10b when the gas flows through the first pipeline 10.
  • the immersion solution J in the embodiment of the present application has high chemical stability and is not easy to chemically react with lithium.
  • the immersion solution J wraps the outer surface of the lithium shavings Li to isolate the lithium shavings Li from the external water or oxygen, and the lithium shavings Li is not prone to spontaneous combustion and fire.
  • the wetting liquid J may be silicone oil, which refers to linear polysiloxane that remains in a liquid state at room temperature.
  • the silicone oil may include at least one of methyl silicone oil and modified silicone oil, wherein the modified silicone oil may include amino-modified silicone oil, epoxy-modified silicone oil, polyether-modified silicone oil, or carboxy-modified silicone oil.
  • the drainage system in the embodiment of the present application may be a negative pressure device, which drains the gas to the gas outlet port 10b under negative pressure.
  • the gas is driven by the drainage system and flows through the inlet end 10a of the first pipeline 10 to the gas outlet end 10b.
  • the gas can drive the immersion liquid J and lithium chips to flow, and the lithium chips When flowing to the infiltration chamber 10c, it can fully contact and infiltrate with the infiltration solution J, and the surface of the lithium chips is wrapped and inerted by the infiltration solution J, which can prevent spontaneous combustion of the lithium chips.
  • the first blocking mechanism 11 can block part of the wetting liquid J, so that the wetting liquid J is blocked, thereby reducing the possibility of the wetting liquid J flowing out of the gas outlet 10b together with the gas.
  • the first pipe 10 and/or the second pipe mentioned in the embodiment of the present application may be a circular pipe, a square pipe or other shaped pipes.
  • the direction shown by X is the vertical direction, that is, the height direction of the first pipeline 10 or the height direction of the second pipeline involved herein .
  • the first blocking mechanism 11 is used to block at least part of the wetting liquid J from flowing out from the gas outlet 10 b.
  • a plurality of first blocking mechanisms 11 can be arranged in sequence along the vertical direction X, and multiple first blocking mechanisms 11 can further reduce the possibility of the immersion liquid J flowing out of the gas outlet 10b together with the gas.
  • the inlet end 10a is located above the gas outlet end 10b in the vertical direction X
  • the first blocking mechanism 11 includes a plurality of blocking plates 111 arranged at intervals, and a gas supply flow is formed between adjacent blocking plates 111 Through the gap 111b, at least part of the blocking plate 111 is inclined relative to the vertical direction X.
  • the gas flows through the barrier plate 111 of the first barrier mechanism 11, it flows out through the gap 111b, and the gas flow drives the wetting liquid J to flow together. Backflow, thereby reducing the wetting liquid J flowing out of the gas outlet 10b with the gas.
  • the projections of adjacent barrier plates 111 along the vertical direction X are connected, that is, the projection surfaces of adjacent barrier plates 111 on the horizontal plane are arranged continuously or partially overlapped.
  • the entire gas in the gap will be blocked by the barrier plates 111 on both sides of the gap 111b and change the flow direction, so as to further reduce the wetting liquid J flowing out of the gas outlet 10b with the gas.
  • the blocking plate 111 includes a plurality of blocking portions 111a, the plurality of blocking portions 111a are connected in sequence, and there is an included angle between two connected blocking portions 111a.
  • the multiple blocking parts 111a can change the flow direction of the gas multiple times, so that the wetting liquid driven by the gas is sequentially blocked by the multiple blocking parts 111a, which can further reduce the flow of the wetting liquid J out of the gas outlet. 10b traffic.
  • the barrier plate 111 may include two or more barrier parts 111a. As the number of barrier parts 111a increases, the number of times the flow direction of the gas is changed increases, and the immersion liquid carried by the gas is absorbed by more barrier parts. 111a can further reduce the wetting liquid J flowing out of the gas outlet 10b with the gas.
  • the blocking portion 111a may extend in the horizontal direction, and as the extension length increases, more immersion fluid J in the horizontal direction is blocked from flowing back.
  • the barrier plate 111 can be directly or indirectly connected to the first pipeline 10 .
  • the barrier plate 111 is disposed on the pipe wall of the first pipe 10 .
  • the first blocking mechanism 11 may further include a connecting plate 112 extending along the vertical direction X, the connecting plate 112 includes a first side 112a and a second side 112b oppositely arranged along the horizontal direction, the second side of the connecting plate 112 One side 112 a is connected to the pipe wall of the first pipe 10 , and a plurality of barrier plates 111 are arranged on the second side 112 b of the connecting plate 112 .
  • a second barrier mechanism 12 is also provided in the infiltration chamber 10c, and the second barrier mechanism 12 is connected to the tube wall of the first pipeline 10 and is located at the first barrier mechanism 11 and the inlet end. Between 10a, the second blocking mechanism 12 is used to block lithium chips from flowing out from the gas outlet 10b. After the lithium chips are inerted by the immersion solution J, part of the lithium chips may flow with the gas, and the second barrier mechanism 12 can block the lithium chips and reduce the lithium chips flowing out through the gas outlet 10b.
  • the second barrier mechanism 12 can be arranged in the immersion liquid J.
  • the density of the lithium chips is lower than that of the immersion liquid J such as silicone oil.
  • Vertical upward buoyancy In order to further prevent lithium chips from flowing out from the gas outlet 10b, the cross-sectional area of the second blocking mechanism 12 on the horizontal plane increases or decreases gradually along the vertical direction. Due to the buoyancy effect of the immersion liquid J, the lithium chips can move smoothly and accumulate in the relatively high part of the second barrier mechanism 12 in the vertical direction, and the lithium chips will basically not affect the relatively high part of the second barrier mechanism 12.
  • the lower portion causes blockage, and gas and immersion fluid J can flow out from the relatively lower portion of the second blocking mechanism 12 .
  • the second blocking mechanism 12 includes two first plates 121 and two second plates 122 .
  • the two second plates 122 are disposed opposite to each other along the second direction Z.
  • the two first plates 121 are arranged opposite to each other along the first direction Y, and the distance between the two first plates 121 gradually increases upward along the vertical direction X, so that the cross-sectional area of the second blocking mechanism 12 on the horizontal plane is along the vertical direction X gradually increases.
  • the distance between the two first boards 121 refers to the distance between the two first boards 121 in the first direction Y.
  • lithium chips Due to the buoyancy of the immersion liquid J, lithium chips are mainly accumulated on the relatively high part of the first plate 121 in the vertical direction X, and the relatively low parts of the first plate 121 and the second plate 122 are basically not covered by lithium chips. Blockage, gas and immersion fluid J can flow out through the first plate 121 and/or the second plate 122 .
  • Both the first direction Y and the second direction Z are parallel to the horizontal plane.
  • the first direction Y is the width direction of the first pipe 10
  • the second direction Z is the length direction of the first pipe 10 .
  • the first direction Y and the second direction Z are both radial directions of the first pipe 10, and the first direction Y and the second direction Z are perpendicular.
  • the second blocking mechanism 12 may be a hollow structure.
  • two first plates 121 and two second plates 122 are connected and enclosed to form a cavity 12a, which can reduce the overall weight of the equipment, so that the equipment is lightweight, and lithium chips are mainly accumulated outside the first plate 121, which is convenient Subsequent collection and treatment of lithium shavings.
  • a through hole 12 b may be opened on the second barrier mechanism 12 .
  • the first plate 121 is provided with a through hole 12b, so that the gas flows out to the gas outlet 10b. Lithium shavings are mainly accumulated on the higher part of the first plate 121 in the vertical direction X.
  • the second plate 122 is provided with a through hole 12b, and the lithium chips mainly gather on the first plate 121, which basically does not cause blockage to the second plate 122, and gas and immersion liquid J flow out through the through hole 12b of the second plate 122.
  • both the first plate 121 and the second plate 122 may be provided with through holes 12b to increase the throughput of gas and immersion liquid J and improve the treatment efficiency of infiltration and inertization of lithium shavings.
  • a filter mechanism 13 is also provided in the infiltration chamber 10c, and the filter mechanism 13 is located between the first blocking mechanism 11 and the gas outlet 10b, and the filter mechanism 13 is used to filter lithium debris and Infiltrate J. After the gas flows through the first barrier mechanism 11, it may still carry some lithium chips and wetting solution J, and the filtering mechanism 13 can further reduce the lithium chips and wetting solution J flowing out of the gas outlet 10b.
  • the filter mechanism 13 may include a plurality of filter elements.
  • the filter mechanism 13 includes a second filter element 131 and a third filter element 132, the second filter element 131 is arranged close to the first blocking mechanism 11, and the third filter element 132 is located at the second filter element 132.
  • the second filter element 131 can be used to filter separated gas and lithium debris.
  • the third filter element 132 can be used to filter the separation gas and the immersion liquid J.
  • the second filter element 131 is connected to the pipe wall of the first pipeline 10, the second filter element 131 has a plurality of first filter holes 131a, and the plurality of first filter holes 131a are arranged at intervals, for example arranged in an array or The uneven arrangement does not limit the arrangement of the first filter holes 131a here.
  • the second blocking mechanism 12 After the lithium scraps are blocked by the second blocking mechanism 12, a part of the lithium scraps may continue to flow with the gas.
  • the aperture of the first filter hole 131a for example, the aperture of the first filter hole 131a is smaller than the particle diameter of the lithium scraps. The lithium debris can be blocked by the first filter hole 131a, and the gas can flow out through the first filter hole 131a.
  • the third filter element 132 may include a multi-layer filter net, and the multi-layer filter net is stacked in sequence along the vertical direction X, and the filter net includes a second filter hole 132a.
  • the filter net includes a second filter hole 132a.
  • the third filter element 132 can filter and separate the gas and the immersion liquid J, and the gas and the immersion liquid J pass through
  • the multi-layer filter is filtered and separated, the infiltration liquid J is blocked by the multi-layer filter, and the gas flows out to the gas outlet end 10b of the first pipeline 10 through the multi-layer filter.
  • the gas still carries lithium shavings, in this case, the gas and lithium shavings will be filtered and separated by a multi-layer filter to further purify the gas.
  • the second filter holes 132a of adjacent filter screens can be arranged in a dislocation, and the immersion liquid J and lithium chips will be further blocked, thereby further improving the gas purification rate.
  • the device for inerting lithium chips further includes a second pipeline 20 and a collection mechanism 21 .
  • the second pipeline 20 is connected to the first pipeline 10
  • the second pipeline 20 includes a liquid inlet 20a and a liquid outlet 20b
  • the liquid inlet 20a is connected to the infiltration chamber 10c.
  • the collection mechanism 21 is connected to the pipe wall of the second pipeline 20, and the collection mechanism 21 is used for separating the immersion liquid J and lithium chips.
  • the infiltration solution J After the lithium chips are infiltrated and inerted by the infiltration solution J in the infiltration cavity 10c of the first pipeline 10, the infiltration solution J is drained into the collection mechanism 21 of the second pipeline 20, and the infiltration solution J will drive the lithium chips to flow into the collection mechanism 21 , The infiltration solution J and the lithium chips can be filtered and separated in the collection mechanism 21, the lithium chips are retained in the collection mechanism 21, and the infiltration solution J flows out of the collection mechanism 21 to achieve the purpose of collecting lithium chips.
  • the collection mechanism 21 includes a collection chamber 211 and a first filter element 212 , and the first filter element 212 is disposed in the collection chamber 211 .
  • the first filter element 212 can trap lithium debris into the collection mechanism 21 , and the infiltration liquid J flows out through the first filter element 212 .
  • the second pipe 20 is a circular pipe, and the collection mechanism 21 forms a collection cavity 211 around the axial direction of the second pipe 20 .
  • connection between the collection mechanism 21 and the second pipeline 20 has various forms.
  • the collection mechanism 21 and the second pipeline 20 can be connected in a detachable manner, which is convenient for removing lithium chips and replacing the collection mechanism 21 .
  • the collection mechanism 21 and the second pipeline 20 can also be fixedly connected, so that the overall structural stability of the device is better.
  • the relative positions of the first pipeline 10 and the second pipeline 20 can be flexibly set according to production conditions.
  • the second pipe 20 can be located below the first pipe 10 in the vertical direction X, and the immersion liquid J and lithium chips can flow from the first pipe 10 to the second pipe 10 by using the gravity of the immersion liquid J and lithium chips themselves.
  • the second pipeline 20 there is no need to additionally arrange other drainage equipment, which can simplify the structure of the device.
  • a first switch 22 can be set in the second pipeline 20, and the first switch 22 is located between the collecting mechanism 21 and the liquid inlet 20a, The first switch 22 is configured to control the connection between the collection mechanism 21 and the infiltration chamber 10c.
  • the first switch 22 controls the collection mechanism 21 to disconnect from the infiltration chamber 10c, the gas drives the flow of lithium chips, and the lithium chips are infiltrated and inerted by the infiltration solution J in the infiltration chamber 10c of the first pipeline 10.
  • the first switch 22 controls the collection mechanism 21 to communicate with the infiltration chamber 10c, and the infiltration solution J flows into the second pipeline 20, and the infiltration solution J drives the lithium chips to flow, and the infiltration solution J flows into the second pipeline 20.
  • J and lithium shavings are filtered and separated by the collection mechanism 21 of the second pipeline 20 .
  • the purified immersion solution J can be further recycled.
  • the lithium scrap inerting treatment device 1 further includes a third pipeline 30, the third pipeline 30 includes a first end 30a and a second end 30b, the first end 30a and the second pipeline 20
  • the outlet end 20b is connected, the second end 30b is connected to the infiltration chamber 10c, and the third pipe 30 is used to transport the infiltration liquid J separated by the collection mechanism 21 to the infiltration chamber 10c.
  • the third pipeline 30 circulates the purified wetting fluid J to the infiltration chamber 10c, thereby improving the utilization rate of the wetting fluid J.
  • a liquid suction pump 31 may be provided between the first end 30a and the second end 30b, and the purified infiltration liquid J is circulated by the liquid suction pump 31 .
  • the second end 30b is located between the gas outlet end 10b and the first blocking mechanism 11 .
  • the purified immersion solution J flows through the first barrier mechanism 11, it can impact the lithium chips adhering to the first barrier mechanism 11 into the immersion solution J, preventing the lithium chips from clogging the first barrier mechanism 11, so that the gas can be discharged smoothly .
  • the second end 30b is located between the gas outlet end 10b and the second filter element 131 .
  • the purified immersion liquid J flows through the second filter element 131, the lithium chips adhering to the second filter element 131 can be impacted into the immersion liquid J, so as to prevent the lithium chips from clogging the second filter element 131 and the first blocking mechanism 11 , so that the gas can be discharged smoothly.
  • the embodiment of the present application also provides a lithium scrap inerting treatment method, please refer to Figure 13, the method includes:
  • the first pipeline includes an inlet end, an infiltration chamber, an outlet end, and an infiltration chamber between the inlet end and the outlet end, the infiltration chamber contains an infiltration liquid, and the first barrier
  • the mechanism is set in the infiltration chamber
  • the first blocking mechanism blocks at least part of the wetting liquid from flowing out from the gas outlet.
  • the first switch 22 controls the infiltration chamber 10 c and the collection mechanism 21 of the second pipeline 20 to be disconnected.
  • the gas is drained into the infiltration solution J in the infiltration chamber 10c through the drainage system, and the gas drives the lithium chips and the infiltration solution to flow.
  • the lithium chips flow through the second blocking mechanism 12, they are blocked and infiltrated and inerted in the infiltration solution J.
  • the immersion liquid J passes through the first blocking mechanism 11 to block backflow, and the gas continues to flow to the filter mechanism 13 , where it is filtered and purified by the filter mechanism 13 and flows out of the gas outlet 10 b of the first pipeline 10 .
  • the first switch 22 controls the communication between the infiltration chamber 10c and the collection mechanism 21 of the second pipeline 20, the infiltration solution J flows and drives the lithium chips to flow into the collection mechanism 21 of the second pipeline 20, and the infiltration solution J passes through the collection mechanism 21 filter purification.
  • the first switch 22 controls the disconnection of the collection mechanism 21 of the infiltration chamber 10c and the second pipeline 20, and the purified infiltration liquid J circulates to the second filter element 131 and the third filter element 13 of the filter mechanism 13 through the third pipeline 30. Between the filter elements 132, the infiltration liquid J flows back into the infiltration chamber 10c.
  • the wetting liquid J in the second pipeline 20 flows back into the wetting cavity 10 c of the first pipeline 10 , and lithium chips are trapped in the collection mechanism 21 .
  • the battery lithium supplement system 100 includes a lithium supplement device 2 and the lithium scrap inerting treatment device 1 of any of the above-mentioned embodiments of the present application, and the lithium scrap
  • the intake end of the inerting treatment device 1 is set opposite to the lithium replenishment device 2 .
  • the lithium replenishment device is used to replenish lithium to the pole piece of the battery.
  • lithium scraps may be generated;
  • the lithium chips are pumped into the infiltration cavity of the lithium chip inerting treatment device 1, the lithium chips are infiltrated in the immersion liquid, and the surface of the lithium chips is wrapped and inerted by the immersion liquid, which can prevent the spontaneous combustion of the lithium chips, etc.
  • the battery lithium supplement system 100 includes a lithium supplement device 2 and the lithium scrap inerting treatment device 1 of any of the above-mentioned embodiments of the present application, and the lithium scrap The intake end of the inerting treatment device 1 is set opposite to the lithium replenishment device 2 .
  • the lithium replenishment device is used to replenish lithium to the pole piece of the battery.

Abstract

The present application provides a lithium chip inerting processing apparatus and processing method, and a battery lithium supplementing system. The lithium chip inerting processing apparatus of the present application comprises: a first pipeline comprising an air inlet end, an air outlet end, and an immersion cavity located between the air inlet end and the air outlet end, the air outlet end being connected to an external drainage system, the drainage system being used to drive a gas containing lithium chips to flow through the first pipeline, and the immersion cavity being used to contain an immersion liquid so as to immerse the lithium chips when the gas flows through the infiltration cavity; and a first blocking mechanism disposed within the infiltration cavity, used to block at least a portion of the immersion liquid from flowing out of the air outlet end as the gas flows through the first pipeline. The present application can significantly improve the safety of battery production.

Description

锂屑惰化处理装置及处理方法、电池补锂系统Lithium shavings inerting treatment device and treatment method, battery lithium replenishment system
相关申请的交叉引用Cross References to Related Applications
本申请要求享有于2021年08月31日提交的名称为“锂屑惰化处理装置及处理方法、电池补锂系统”的中国专利申请202111011270.9的优先权,该申请的全部内容通过引用并入本文中。This application claims the priority of the Chinese patent application 202111011270.9 entitled "Inerting Lithium Shavings Treatment Device and Treatment Method, Battery Lithium Supplementation System" filed on August 31, 2021, the entire content of which is incorporated herein by reference middle.
技术领域technical field
本申请涉及电池生产技术领域,特别是涉及一种锂屑惰化处理装置及处理方法、电池补锂系统。The present application relates to the technical field of battery production, in particular to a lithium scrap inerting treatment device and treatment method, and a battery lithium replenishment system.
背景技术Background technique
锂离子电池单体广泛用于电子设备,例如手机、笔记本电脑、电瓶车、电动汽车、电动飞机、电动轮船、电动玩具汽车、电动玩具轮船、电动玩具飞机和电动工具等等。Lithium-ion battery cells are widely used in electronic equipment, such as mobile phones, laptop computers, battery cars, electric vehicles, electric aircraft, electric ships, electric toy cars, electric toy ships, electric toy planes and electric tools, etc.
在锂离子电池的生产过程中,可能会产生锂屑,而锂屑容易引发安全问题。如何增强电池单体生产的安全性,是电池技术中一个亟待解决的技术问题。In the production process of lithium-ion batteries, lithium shavings may be produced, and lithium shavings are likely to cause safety problems. How to enhance the safety of battery cell production is an urgent technical problem in battery technology.
发明内容Contents of the invention
本申请提供了一种锂屑惰化处理装置及处理方法、电池补锂系统,旨在提高电池生产的安全性。The present application provides a lithium scrap inerting treatment device and treatment method, and a battery lithium replenishment system, aiming at improving the safety of battery production.
第一方面,本申请实施例提供了一种锂屑惰化处理装置,包括:第一管道,包括进气端、出气端和位于进气端和出气端之间的浸润腔,出气端用于与外部的引流系统连接,引流系统用于带动包含锂屑的气体流过第一管道,浸润腔用于容纳浸润液,以在气体流经浸润腔时浸润锂屑;以及第一阻隔机构,设置于浸润腔内,并用于在气体流过第一管道时阻挡至少部分浸润液从出气端流出。In the first aspect, an embodiment of the present application provides a device for inerting lithium scraps, including: a first pipeline, including an inlet end, an outlet end, and an infiltration chamber between the inlet end and the outlet end, and the outlet end is used for Connected with an external drainage system, the drainage system is used to drive the gas containing lithium chips to flow through the first pipeline, the infiltration chamber is used to accommodate the infiltration liquid, so as to infiltrate the lithium chips when the gas flows through the infiltration chamber; and the first blocking mechanism is set It is in the wetting chamber, and is used to block at least part of the wetting liquid from flowing out from the gas outlet when the gas flows through the first pipeline.
上述方案中,气体在引流系统的带动下,经第一管道的进气端流至出气端,在气体流动过程中,气体能够带动浸润液和锂屑流动,锂屑流至浸润腔时,与浸润液接触并被浸润液所浸润,锂屑的表面被浸润液包裹惰化,可防止锂屑发生自燃等现象。同时,第一阻隔机构能够阻挡部分浸润液,以使浸润液被阻挡回流,进而降低浸润液随气体一同流出出气端的可能性。In the above scheme, driven by the drainage system, the gas flows from the inlet end of the first pipeline to the gas outlet end. During the gas flow process, the gas can drive the immersion liquid and lithium chips to flow. When the lithium chips flow to the infiltration chamber, the The immersion liquid is in contact with and infiltrated by the immersion liquid, and the surface of the lithium shavings is wrapped and inert by the immersion liquid, which can prevent spontaneous combustion of the lithium shavings. At the same time, the first blocking mechanism can block part of the wetting liquid, so that the wetting liquid is blocked from flowing back, thereby reducing the possibility of the wetting liquid flowing out of the gas outlet together with the gas.
在一些实施例中,进气端位于出气端竖直方向的上方,第一阻隔机构包括多个间隔设置的阻隔板,相邻的阻隔板之间形成供气体流过的间隙,阻隔板的至少部分相对于竖直方向倾斜。本申请实施例的气体流经第一阻隔机构的阻隔板时,经间隙流 出,气体带动浸润液一同流动,阻隔板倾斜的部分能够改变气体的流向,以阻挡浸润液并使浸润液回流,进而降低浸润液随气体流出出气端的可能性。In some embodiments, the inlet end is located above the gas outlet end in the vertical direction, and the first blocking mechanism includes a plurality of blocking plates arranged at intervals, gaps for gas flow are formed between adjacent blocking plates, and at least Parts are inclined relative to the vertical. When the gas in the embodiment of the present application flows through the barrier plate of the first barrier mechanism, it flows out through the gap, and the gas drives the immersion liquid to flow together. The inclined part of the barrier plate can change the flow direction of the gas to block the immersion liquid and make the immersion liquid flow back, and then Reduce the possibility of wetting liquid flowing out of the gas outlet with the gas.
在一些实施例中,阻隔板包括多个阻隔部,多个阻隔部依次连接,相连的两个阻隔部之间具有夹角。本申请实施例的气体流经第一阻隔机构时,多个阻隔部可以多次的改变气体的流向,使气体所带动的浸润液被多个阻隔部所阻挡,可以进一步降低减少随气体流出出气端的浸润液。In some embodiments, the barrier plate includes a plurality of barrier parts, the multiple barrier parts are connected in sequence, and there is an included angle between two connected barrier parts. When the gas in the embodiment of the present application flows through the first blocking mechanism, the multiple blocking parts can change the flow direction of the gas multiple times, so that the infiltration liquid driven by the gas is blocked by the multiple blocking parts, which can further reduce the outflow of gas with the gas. terminal immersion fluid.
在一些实施例中,相邻阻隔板沿竖直方向的投影相连。本申请实施例的气体于间隙流动时,间隙内的气体整体会受到间隙两侧的阻隔板的阻挡并改变流向,以此进一步减少随气体流出出气端的浸润液。In some embodiments, the projections of adjacent barrier panels along the vertical direction are connected. When the gas in the embodiment of the present application flows through the gap, the gas in the gap as a whole will be blocked by the barrier plates on both sides of the gap and change the flow direction, so as to further reduce the wetting liquid flowing out of the gas outlet with the gas.
在一些实施例中,浸润腔内还设置有第二阻隔机构,第二阻隔机构连接于第一管道的管壁,并位于第一阻隔机构和进气端之间,第二阻隔机构用于阻挡锂屑从出气端流出。锂屑经过浸润液的惰化处理后,一部分锂屑可能会随着气体继续流动,而本申请实施例的第二阻隔机构可以起到阻挡锂屑的作用,可减少经由出气端流出的锂屑。In some embodiments, a second blocking mechanism is also provided in the infiltration chamber, the second blocking mechanism is connected to the pipe wall of the first pipeline, and is located between the first blocking mechanism and the inlet end, and the second blocking mechanism is used to block Lithium chips flow out from the gas outlet. After the lithium chips are inerted by the immersion liquid, some lithium chips may continue to flow with the gas, but the second barrier mechanism in the embodiment of the present application can block the lithium chips and reduce the flow of lithium chips through the gas outlet. .
在一些实施例中,第二阻隔机构在水平面的截面积沿竖直方向逐渐增大或减小。锂屑的密度相较于浸润液的密度更小,锂屑由于受到浸润液的浮力作用会有上浮的趋势,锂屑聚积于第二阻隔机构在竖直方向上的相对较高的部分,锂屑基本不会对第二阻隔机构的相对较低的部分造成堵塞,气体可以带动浸润液从第二阻隔机构的相对较低的部分流出。In some embodiments, the cross-sectional area of the second blocking mechanism on the horizontal plane gradually increases or decreases along the vertical direction. The density of lithium chips is smaller than that of the immersion liquid. Lithium chips have a tendency to float up due to the buoyancy of the immersion liquid. Lithium chips accumulate in the relatively high vertical part of the second barrier mechanism. The swarf basically does not block the relatively lower part of the second barrier mechanism, and the gas can drive the immersion liquid to flow out from the relatively lower part of the second barrier mechanism.
在一些实施例中,第二阻隔机构包括:沿第一方向相对设置的两个第一板,两个第一板之间的间距沿竖直方向向上逐渐增大;以及沿第二方向相对设置的两个第二板,两个第一板和两个第二板连接并围合形成空腔,第一板和/或第二板设置有多个通孔,以使气体和浸润液流出,第一方向和第二方向均与水平面平行,第一方向和第二方向垂直。在本申请实施例中,通孔可以起到过滤锂屑的作用,同时,锂屑主要聚积于第一板竖直方向上相对较高的部分的外侧,第一板和第二板的相对较低的部分不会被锂屑堵塞,气体可以带动浸润液经第一板和/或第二板流出。In some embodiments, the second blocking mechanism includes: two first plates disposed opposite to each other along the first direction, the distance between the two first plates gradually increases upward along the vertical direction; and two first plates disposed opposite to each other along the second direction The two second plates, the two first plates and the two second plates are connected and enclosed to form a cavity, the first plate and/or the second plate are provided with a plurality of through holes to allow the gas and immersion liquid to flow out, Both the first direction and the second direction are parallel to the horizontal plane, and the first direction and the second direction are perpendicular. In the embodiment of the present application, the through hole can play the role of filtering lithium chips. At the same time, the lithium chips are mainly accumulated on the outside of the relatively higher part of the first plate in the vertical direction, and the relatively small parts of the first plate and the second plate The lower part will not be blocked by lithium shavings, and the gas can drive the immersion liquid to flow out through the first plate and/or the second plate.
在一些实施例中,浸润腔内还设置有过滤机构,过滤机构位于第一阻隔机构和出气端之间,并用于过滤气体中的锂屑和浸润液。本申请实施例的气体流经第一阻隔机构后,仍可能会携带部分锂屑和浸润液,经过过滤机构的过滤作用,可以进一步减少流出出气端的锂屑和浸润液。In some embodiments, a filter mechanism is also provided in the infiltration chamber, and the filter mechanism is located between the first blocking mechanism and the gas outlet, and is used to filter lithium debris and immersion liquid in the gas. After the gas in the embodiment of the present application flows through the first barrier mechanism, it may still carry part of the lithium debris and the wetting liquid, and the filtering function of the filtering mechanism can further reduce the lithium debris and the wetting fluid flowing out of the gas outlet.
在一些实施例中,锂屑惰化处理装置还包括:第二管道,第二管道和第一管道连接,第二管道包括进液端和出液端,进液端和浸润腔连接;以及收集机构,收集机构连接于第二管道的管壁,收集机构用于分离浸润液和锂屑。在本申请实施例中,锂屑经第一管道的浸润腔内的浸润液浸润惰化后,将包含锂屑的浸润液引流至第二管道的收集机构内,并将浸润液和锂屑过滤分离,锂屑留存至收集机构内,达到对锂屑收集的目的。In some embodiments, the lithium scrap inerting treatment device also includes: a second pipeline, the second pipeline is connected to the first pipeline, the second pipeline includes a liquid inlet and a liquid outlet, and the liquid inlet is connected to the infiltration chamber; and the collection The collection mechanism is connected to the pipe wall of the second pipeline, and the collection mechanism is used to separate the immersion liquid and lithium chips. In the embodiment of the present application, after the lithium chips are infiltrated and inerted by the infiltration solution in the infiltration cavity of the first pipeline, the infiltration solution containing lithium chips is drained into the collection mechanism of the second pipeline, and the infiltration solution and lithium chips are filtered Separation, the lithium scraps are retained in the collection mechanism to achieve the purpose of collecting lithium scraps.
在一些实施例中,第二管道在竖直方向上位于第一管道的下方。本申请实施例利用浸润液和锂屑自身的重力作用,使浸润液和锂屑可以从第一管道流至第二管道 内,不需额外设置其他引流设备,可以简化装置的结构。In some embodiments, the second conduit is located vertically below the first conduit. The embodiment of the present application uses the gravity of the immersion liquid and lithium chips to allow the immersion liquid and lithium chips to flow from the first pipeline to the second pipeline without additional drainage equipment, which can simplify the structure of the device.
在一些实施例中,收集机构包括收集腔和第一过滤件,第一过滤件设置于收集腔,并用于分离浸润液和锂屑。In some embodiments, the collection mechanism includes a collection chamber and a first filter, and the first filter is disposed in the collection chamber and used to separate the immersion liquid and lithium debris.
在一些实施例中,第二管道内还设置有第一开关,第一开关位于收集机构和进液端之间,第一开关被配置为控制收集机构与浸润腔的通断。本申请实施例利用第一开关可以调节第一管道和第二管道的生产节奏。In some embodiments, a first switch is further arranged in the second pipeline, the first switch is located between the collection mechanism and the liquid inlet, and the first switch is configured to control the connection between the collection mechanism and the infiltration chamber. In the embodiment of the present application, the production rhythm of the first pipeline and the second pipeline can be adjusted by using the first switch.
在一些实施例中,收集机构可拆卸设置于第二管道内。本申请实施例的收集机构和第二管道之间可采用可拆卸方式连接,便于取出锂屑、更换收集机构。In some embodiments, the collection mechanism is detachably disposed in the second conduit. The collection mechanism in the embodiment of the present application and the second pipeline can be connected in a detachable manner, which is convenient for removing lithium chips and replacing the collection mechanism.
在一些实施例中,锂屑惰化处理装置还包括第三管道,第三管道包括第一端和第二端,第一端与第二管道的出液端连接,第二端与浸润腔连接,第三管道用于将收集机构分离出的浸润液输送到浸润腔。在本申请实施例中,浸润液经第二管道的收集机构净化后,第三管道将净化后的浸润液循环至浸润腔,以此提高浸润液的利用率。In some embodiments, the lithium scrap inerting treatment device further includes a third pipeline, the third pipeline includes a first end and a second end, the first end is connected to the liquid outlet of the second pipeline, and the second end is connected to the infiltration chamber , the third pipeline is used to transport the infiltration fluid separated by the collection mechanism to the infiltration chamber. In the embodiment of the present application, after the infiltration fluid is purified by the collection mechanism of the second pipeline, the third pipeline circulates the purified infiltration fluid to the infiltration cavity, thereby improving the utilization rate of the infiltration fluid.
在一些实施例中,第二端位于出气端和第一阻隔机构之间。在本申请实施例中,净化后的浸润液流经第一阻隔机构时,可以将粘附于第一阻隔机构的锂屑冲击至浸润液中,避免锂屑堵塞第一阻隔机构,使气体能够顺畅排出。In some embodiments, the second end is located between the outlet end and the first barrier mechanism. In the embodiment of the present application, when the purified immersion liquid flows through the first barrier mechanism, the lithium chips adhering to the first barrier mechanism can be impacted into the immersion liquid to prevent the lithium chips from blocking the first barrier mechanism, so that the gas can Discharge smoothly.
第二方面,本申请实施例提供了一种电池补锂系统,包括:补锂装置;以及如第一方面任一实施例的锂屑惰化处理装置,锂屑惰化处理装置的进气端与补锂装置相对设置。补锂装置用于对电池的极片进行补锂,在补锂的过程中,可能会产生锂屑;本申请实施例的锂屑惰化处理装置的进气端与补锂装置相对设置,以在补锂的过程中将锂屑抽入到浸润腔内,锂屑在浸润液中被浸润,锂屑的表面被浸润液包裹惰化,可防止锂屑发生自燃等现象。In the second aspect, an embodiment of the present application provides a battery lithium replenishment system, including: a lithium replenishment device; It is set opposite to the lithium supplementation device. The lithium replenishing device is used to replenish lithium to the pole piece of the battery. During the lithium replenishing process, lithium scraps may be generated; In the process of lithium replenishment, the lithium chips are pumped into the infiltration chamber, the lithium chips are infiltrated in the infiltration solution, and the surface of the lithium chips is wrapped and inerted by the infiltration solution, which can prevent spontaneous combustion of the lithium chips.
第三方面,本申请实施例提供了一种锂屑惰化处理方法,包括:提供第一管道和第一阻隔机构,第一管道包括进气端、出气端和位于进气端和出气端之间的浸润腔,浸润腔内容纳有浸润液,第一阻隔机构设置于浸润腔内;将引流系统与出气端连接,并利用引流系统带动包含锂屑的气体流过第一管道,气体流经浸润腔时浸润锂屑,其中,在气体流过第一管道时,第一阻隔机构阻挡至少部分浸润液从出气端流出。In a third aspect, an embodiment of the present application provides a lithium scrap inerting treatment method, including: providing a first pipeline and a first barrier mechanism, the first pipeline includes an inlet end, an outlet end, and a gas outlet located between the inlet end and the outlet end. The infiltration chamber contains the infiltration liquid, and the first barrier mechanism is set in the infiltration chamber; the drainage system is connected to the gas outlet, and the drainage system is used to drive the gas containing lithium chips to flow through the first pipeline, and the gas flows through the Lithium shavings are infiltrated when the cavity is infiltrated, wherein, when the gas flows through the first pipeline, the first blocking mechanism blocks at least part of the infiltrating liquid from flowing out from the gas outlet.
附图说明Description of drawings
下面将参考附图来描述本申请示例性实施例的特征、优点和技术效果。The features, advantages, and technical effects of the exemplary embodiments of the present application will be described below with reference to the accompanying drawings.
图1是本申请一些实施例提供的锂屑惰化处理装置的结构示意图;Figure 1 is a schematic structural view of a lithium scrap inerting treatment device provided in some embodiments of the present application;
图2是本申请一些实施例提供的锂屑惰化处理装置的第一阻隔机构的结构示意图;Fig. 2 is a schematic structural view of the first barrier mechanism of the lithium scrap inerting treatment device provided by some embodiments of the present application;
图3是图2所示的第一阻隔机构在另一角度下的结构示意图;Fig. 3 is a structural schematic view of the first blocking mechanism shown in Fig. 2 at another angle;
图4是图2所示的第一阻隔机构在又一角度下的结构示意图;Fig. 4 is a structural schematic view of the first blocking mechanism shown in Fig. 2 at another angle;
图5是本申请另一些实施例提供的锂屑惰化处理装置的结构示意图;Fig. 5 is a schematic structural view of a lithium scrap inerting treatment device provided in other embodiments of the present application;
图6是本申请一些实施例提供的锂屑惰化处理装置的第二阻隔机构的结构示意 图;Fig. 6 is a schematic structural view of the second barrier mechanism of the lithium scrap inerting treatment device provided in some embodiments of the present application;
图7是图6所示的第二阻隔机构在另一角度下的结构示意图;Fig. 7 is a structural schematic diagram of the second blocking mechanism shown in Fig. 6 at another angle;
图8是本申请又一些实施例提供的锂屑惰化处理装置的结构示意图;Fig. 8 is a schematic structural diagram of a lithium scrap inerting treatment device provided in some other embodiments of the present application;
图9是本申请一些实施例提供的锂屑惰化处理装置的第二过滤件的结构示意图;Fig. 9 is a schematic structural view of the second filter element of the lithium scrap inerting treatment device provided in some embodiments of the present application;
图10是本申请一些实施例提供的锂屑惰化处理装置的第三过滤件的结构示意图;Fig. 10 is a schematic structural view of the third filter element of the lithium scrap inerting treatment device provided in some embodiments of the present application;
图11是图10所示的第三过滤件在另一角度下的结构示意图;Fig. 11 is a schematic structural view of the third filter shown in Fig. 10 at another angle;
图12是本申请再一些实施例提供的锂屑惰化处理装置的结构示意图;Fig. 12 is a schematic structural diagram of a lithium scrap inerting treatment device provided in some further embodiments of the present application;
图13是本申请一些实施例提供的锂屑惰化处理方法的流程示意图;Fig. 13 is a schematic flow diagram of a lithium scrap inerting treatment method provided in some embodiments of the present application;
图14是本申请一些实施例提供的处于一种工作状态的锂屑惰化处理装置的结构示意图;Fig. 14 is a schematic structural diagram of a lithium scrap inerting treatment device in a working state provided by some embodiments of the present application;
图15是本申请一些实施例提供的处于另一种工作状态的锂屑惰化处理装置的结构示意图;Fig. 15 is a schematic structural diagram of a lithium scrap inerting treatment device in another working state provided by some embodiments of the present application;
图16是本申请一些实施例提供的处于又一种工作状态的锂屑惰化处理装置的结构示意图;Fig. 16 is a schematic structural diagram of a lithium scrap inerting treatment device in another working state provided by some embodiments of the present application;
图17是本申请一些实施例提供的处于再一种工作状态的锂屑惰化处理装置的结构示意图;Fig. 17 is a schematic structural diagram of a lithium scrap inerting treatment device in another working state provided by some embodiments of the present application;
图18是本申请一些实施例提供的电池补锂系统的结构示意图。Fig. 18 is a schematic structural diagram of a battery lithium replenishment system provided by some embodiments of the present application.
附图并未按照实际的比例绘制。The figures are not drawn to scale.
图中各附图标记:Each reference sign in the figure:
X、竖直方向;Y、第一方向;Z、第二方向;X, vertical direction; Y, first direction; Z, second direction;
1、锂屑惰化处理装置,2、补锂装置;J、浸润液;Li、锂屑;1. Lithium shavings inerting treatment device, 2. Lithium replenishment device; J, immersion solution; Li, lithium shavings;
10、第一管道;10a、进气端;10b、出气端;10c、浸润腔;10. The first pipeline; 10a, the air inlet end; 10b, the air outlet end; 10c, the infiltration chamber;
11、第一阻隔机构;111、阻隔板;111a、阻隔部;111b、间隙;112、连接板;112a、第一侧;112b、第二侧;11. The first blocking mechanism; 111, the blocking plate; 111a, the blocking part; 111b, the gap; 112, the connecting plate; 112a, the first side; 112b, the second side;
12、第二阻隔机构,121、第一板;122、第二板;12a、空腔;12b、通孔;12. The second blocking mechanism, 121, the first plate; 122, the second plate; 12a, the cavity; 12b, the through hole;
13、过滤机构;131、第二过滤件;131a、第一过滤孔;132、第三过滤件;132a、第二过滤孔;13. Filter mechanism; 131, second filter element; 131a, first filter hole; 132, third filter element; 132a, second filter hole;
20、第二管道;20a、进液端;20b、出液端;21、收集机构;211、收集腔;212、第一过滤件;22、第一开关;20. Second pipeline; 20a, liquid inlet; 20b, liquid outlet; 21, collection mechanism; 211, collection chamber; 212, first filter; 22, first switch;
30、第三管道;30a、第一端;30b、第二端;31、吸液泵。30. The third pipeline; 30a, the first end; 30b, the second end; 31. The suction pump.
具体实施方式Detailed ways
下面结合附图和实施例对本申请的实施方式作进一步详细描述。以下实施例的详细描述和附图用于示例性地说明本申请的原理,但不能用来限制本申请的范围,即本申请不限于所描述的实施例。The implementation manner of the present application will be further described in detail below with reference to the drawings and embodiments. The detailed description and drawings of the following embodiments are used to illustrate the principles of the application, but not to limit the scope of the application, that is, the application is not limited to the described embodiments.
在本申请的描述中,需要说明的是,除非另有说明,“多个”的含义是两个以上;术语“上”、“下”、“左”、“右”、“内”、“外”等指示的方位或位置关系仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。此外,术语“第一”、“第二”、“第三”等仅用于描述目的,而不能理解为指示或暗示相对重要性。“垂直”并不是严格意义上的垂直,而是在误差允许范围之内。“平行”并不是严格意义上的平行,而是在误差允许范围之内。In the description of this application, it should be noted that, unless otherwise specified, the meaning of "plurality" is more than two; the terms "upper", "lower", "left", "right", "inner", " The orientation or positional relationship indicated by "outside" and so on are only for the convenience of describing the present application and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a reference to this application. Application Restrictions. In addition, the terms "first", "second", "third", etc. are used for descriptive purposes only and should not be construed as indicating or implying relative importance. "Vertical" is not strictly vertical, but within the allowable range of error. "Parallel" is not strictly parallel, but within the allowable range of error.
在本申请的描述中,还需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是直接相连,也可以通过中间媒介间接相连。对于本领域的普通技术人员而言,可视具体情况理解上述术语在本申请中的具体含义。In the description of this application, it should also be noted that, unless otherwise clearly specified and limited, the terms "installation", "connection", and "connection" should be interpreted in a broad sense, for example, it can be a fixed connection or a flexible connection. Disassembled connection, or integral connection; it can be directly connected or indirectly connected through an intermediary. For those of ordinary skill in the art, the specific meanings of the above terms in this application can be understood according to specific situations.
本申请中,电池单体可以包括锂离子二次电池单体、锂离子一次电池单体、锂硫电池单体或钠锂离子电池单体等,本申请实施例对此并不限定。In the present application, the battery cells may include lithium-ion secondary battery cells, lithium-ion primary battery cells, lithium-sulfur battery cells, or sodium-lithium-ion battery cells, which are not limited in the embodiments of the present application.
电池单体包括电极组件和电解液,电极组件由极片和隔离件组件。极片包括正极片和负极片。电池单体主要依靠金属离子例如锂离子在正极片和负极片之间移动来工作。正极片包括正极集流体和正极活性物质层,正极活性物质层涂覆于正极集流体的表面,未涂敷正极活性物质层的正极集流体凸出于已涂覆正极活性物质层的正极集流体,未涂敷正极活性物质层的正极集流体作为正极极耳。以锂离子电池为例,正极集流体的材料可以为铝,正极活性物质可以为钴酸锂、磷酸铁锂、三元锂或锰酸锂等。负极片包括负极集流体和负极活性物质层,负极活性物质层涂覆于负极集流体的表面,未涂敷负极活性物质层的负极集流体凸出于已涂覆负极活性物质层的负极集流体,未涂敷负极活性物质层的负极集流体作为负极极耳。负极集流体的材料可以为铜,负极活性物质可以为碳或硅等。The battery cell includes an electrode assembly and an electrolyte, and the electrode assembly is composed of a pole piece and a separator assembly. The pole pieces include positive pole pieces and negative pole pieces. A battery cell primarily relies on the movement of metal ions, such as lithium ions, between the positive and negative plates. The positive electrode sheet includes a positive electrode current collector and a positive electrode active material layer, the positive electrode active material layer is coated on the surface of the positive electrode current collector, and the positive electrode current collector that is not coated with the positive electrode active material layer protrudes from the positive electrode collector that has been coated with the positive electrode active material layer , the positive electrode current collector not coated with the positive electrode active material layer is used as the positive electrode tab. Taking a lithium-ion battery as an example, the material of the positive electrode current collector can be aluminum, and the positive electrode active material can be lithium cobaltate, lithium iron phosphate, ternary lithium or lithium manganate. The negative electrode sheet includes a negative electrode current collector and a negative electrode active material layer, the negative electrode active material layer is coated on the surface of the negative electrode current collector, and the negative electrode current collector that is not coated with the negative electrode active material layer protrudes from the negative electrode collector that has been coated with the negative electrode active material layer , the negative electrode current collector not coated with the negative electrode active material layer is used as the negative electrode tab. The material of the negative electrode current collector may be copper, and the negative electrode active material may be carbon or silicon.
电池技术的发展要同时考虑多方面的设计因素,例如,能量密度、循环寿命、放电容量、充放电倍率等性能参数,另外,还需考虑安全性能。The development of battery technology should consider many design factors at the same time, such as energy density, cycle life, discharge capacity, charge and discharge rate and other performance parameters. In addition, safety performance must also be considered.
电池单体在首次充放电过程中,会形成固体电解质膜(solid electrolyte interphase,SEI膜),而SEI膜的形成会消耗部分锂,如此将会造成锂的损失,从而使得电池单体的放电容量和首次充放电倍率降低。为了减少电池单体在首次充电过程中电池容量的不可逆降低,通常在极片成型过程中,采用补锂装置在极片的表面补充活性锂,将补锂后的极片应用于电池单体,以此提高电池单体的放电容量和首次充放电倍率。During the first charge and discharge process of the battery cell, a solid electrolyte film (solid electrolyte interphase, SEI film) will be formed, and the formation of the SEI film will consume part of the lithium, which will cause the loss of lithium, thereby reducing the discharge capacity of the battery cell. And the first charge and discharge rate is reduced. In order to reduce the irreversible decrease in the battery capacity of the battery cell during the first charging process, a lithium replenishing device is usually used to replenish active lithium on the surface of the pole piece during the forming process of the pole piece, and the pole piece after lithium supplementation is applied to the battery cell. In this way, the discharge capacity and initial charge-discharge rate of the battery cell can be improved.
极片的补锂工艺主要包括压延工艺和覆合工艺,压延工艺是通过辊压将锂带压薄以形成锂膜,覆合工艺则是通过辊压将锂膜覆合到极片的表面。The lithium replenishment process of the pole piece mainly includes the calendering process and the lamination process. The calendering process is to thin the lithium strip by rolling to form a lithium film, and the lamination process is to laminate the lithium film to the surface of the pole piece by rolling.
申请人发现,在补锂过程中会产生锂屑,需要对锂屑收集处理。由于锂的化学性质较为活泼,在收集处理锂屑的过程中通常会发生锂屑自燃等问题,引发安全风险。The applicant found that lithium scraps are generated during the lithium supplementation process, and lithium scraps need to be collected and processed. Due to the relatively active chemical properties of lithium, problems such as spontaneous combustion of lithium scraps usually occur during the process of collecting and processing lithium scraps, causing safety risks.
基于申请人发现的上述问题,申请人提出了一种锂屑惰化处理装置。该锂屑惰化处理装置可以用于收集处理补锂过程所产生的锂屑,并可以保证收集处理锂屑过程 的安全性。当然,该锂屑惰化处理装置也可以用于收集处理其它生产工序所产生的锂屑。Based on the above-mentioned problems discovered by the applicant, the applicant proposed a device for inerting lithium shavings. The lithium scrap inerting treatment device can be used to collect and process lithium scrap produced in the process of lithium supplementation, and can ensure the safety of the process of collecting and processing lithium scrap. Of course, the lithium scrap inerting treatment device can also be used to collect and process lithium scrap produced in other production processes.
为了更好地理解本申请,下面结合图1至图18对本申请实施例进行描述。In order to better understand the present application, the following describes the embodiment of the present application with reference to FIG. 1 to FIG. 18 .
请参阅图1,本申请实施例提供的一种锂屑惰化处理装置,包括第一管道10,包括进气端10a、出气端10b和位于进气端10a和出气端10b之间的浸润腔10c,出气端10b用于与外部的引流系统连接,引流系统用于带动包含锂屑Li的气体流过第一管道10,浸润腔10c用于容纳浸润液J,以在气体流经浸润腔10c时浸润锂屑Li。第一阻隔机构11,设置于浸润腔10c内,并用于在气体流过第一管道10时阻挡至少部分浸润液J从出气端10b流出。Please refer to FIG. 1 , a lithium scrap inerting treatment device provided by an embodiment of the present application includes a first pipeline 10, including an inlet end 10a, an outlet end 10b, and an infiltration chamber between the inlet end 10a and the outlet end 10b. 10c, the gas outlet 10b is used to connect with the external drainage system, the drainage system is used to drive the gas containing lithium chips Li to flow through the first pipeline 10, and the infiltration chamber 10c is used to accommodate the infiltration liquid J, so that when the gas flows through the infiltration chamber 10c When infiltrating lithium chips Li. The first blocking mechanism 11 is arranged in the infiltration chamber 10c, and is used for blocking at least part of the infiltration liquid J from flowing out from the gas outlet end 10b when the gas flows through the first pipeline 10.
本申请实施例的浸润液J具有较高的化学稳定性,不容易与锂发生化学反应,浸润液J包裹于锂屑Li的外表面,将锂屑Li和外部的水或氧隔绝,锂屑Li不易发生自燃起火。示例性地,浸润液J可以为硅油,硅油是指在室温下保持液体状态的线性聚硅氧烷。硅油可以包括甲基硅油和改性硅油中的至少一种,其中,改性硅油可以包括氨基改性硅油、环氧基改性硅油、聚醚改性硅油或羧基改性硅油等。The immersion solution J in the embodiment of the present application has high chemical stability and is not easy to chemically react with lithium. The immersion solution J wraps the outer surface of the lithium shavings Li to isolate the lithium shavings Li from the external water or oxygen, and the lithium shavings Li is not prone to spontaneous combustion and fire. Exemplarily, the wetting liquid J may be silicone oil, which refers to linear polysiloxane that remains in a liquid state at room temperature. The silicone oil may include at least one of methyl silicone oil and modified silicone oil, wherein the modified silicone oil may include amino-modified silicone oil, epoxy-modified silicone oil, polyether-modified silicone oil, or carboxy-modified silicone oil.
本申请实施例的引流系统可以为负压设备,将气体负压引流至出气端10b。The drainage system in the embodiment of the present application may be a negative pressure device, which drains the gas to the gas outlet port 10b under negative pressure.
由于锂屑密度小于浸润液,如直接将锂屑收集至浸润液内,锂屑可能会直接浮起于浸润液表面,造成锂屑不能被充分浸润惰化。在本申请实施例中,气体在引流系统的带动下,经第一管道10的进气端10a流至出气端10b,在气体流动过程中,气体能够带动浸润液J和锂屑流动,锂屑流至浸润腔10c时,能够与浸润液J充分接触浸润,锂屑的表面被浸润液J包裹惰化,可防止锂屑发生自燃等现象。同时,第一阻隔机构11能够阻挡部分浸润液J,以使浸润液J被阻挡,进而降低浸润液J随气体一同流出出气端10b的可能性。需要指出的是,本申请实施例所提及的第一管道10和/或第二管道可以为圆形管道、方形管道或其它形状的管道。Since the density of lithium chips is smaller than that of the immersion solution, if the lithium chips are directly collected into the immersion solution, the lithium chips may directly float on the surface of the immersion solution, resulting in insufficient infiltration and inerting of the lithium chips. In the embodiment of the present application, the gas is driven by the drainage system and flows through the inlet end 10a of the first pipeline 10 to the gas outlet end 10b. During the gas flow process, the gas can drive the immersion liquid J and lithium chips to flow, and the lithium chips When flowing to the infiltration chamber 10c, it can fully contact and infiltrate with the infiltration solution J, and the surface of the lithium chips is wrapped and inerted by the infiltration solution J, which can prevent spontaneous combustion of the lithium chips. At the same time, the first blocking mechanism 11 can block part of the wetting liquid J, so that the wetting liquid J is blocked, thereby reducing the possibility of the wetting liquid J flowing out of the gas outlet 10b together with the gas. It should be pointed out that the first pipe 10 and/or the second pipe mentioned in the embodiment of the present application may be a circular pipe, a square pipe or other shaped pipes.
本申请实施例所提及的方向请参照图1中所示的坐标系,X所示的方向为竖直方向,即第一管道10的高度方向或者本文中所涉及的第二管道的高度方向。Please refer to the coordinate system shown in Figure 1 for the directions mentioned in the embodiments of the present application. The direction shown by X is the vertical direction, that is, the height direction of the first pipeline 10 or the height direction of the second pipeline involved herein .
在一些实施例中,请参阅图1至图4,第一阻隔机构11用于阻隔至少部分浸润液J从出气端10b流出。第一阻隔机构11可以沿竖直方向X依次设置多个,多个第一阻隔机构11可以进一步降低浸润液J随气体一同流出出气端10b的可能性。In some embodiments, please refer to FIG. 1 to FIG. 4 , the first blocking mechanism 11 is used to block at least part of the wetting liquid J from flowing out from the gas outlet 10 b. A plurality of first blocking mechanisms 11 can be arranged in sequence along the vertical direction X, and multiple first blocking mechanisms 11 can further reduce the possibility of the immersion liquid J flowing out of the gas outlet 10b together with the gas.
请参阅图1和图2,进气端10a位于出气端10b竖直方向X的上方,第一阻隔机构11包括多个间隔设置的阻隔板111,相邻的阻隔板111之间形成供气体流过的间隙111b,阻隔板111的至少部分相对于竖直方向X倾斜。气体流经第一阻隔机构11的阻隔板111时,经间隙111b流出,气体流动带动浸润液J一同流动,阻隔板111倾斜的部分能够改变气体的流向,以阻挡浸润液J并使浸润液J回流,进而减少随气体流出出气端10b的浸润液J。Referring to Fig. 1 and Fig. 2, the inlet end 10a is located above the gas outlet end 10b in the vertical direction X, the first blocking mechanism 11 includes a plurality of blocking plates 111 arranged at intervals, and a gas supply flow is formed between adjacent blocking plates 111 Through the gap 111b, at least part of the blocking plate 111 is inclined relative to the vertical direction X. When the gas flows through the barrier plate 111 of the first barrier mechanism 11, it flows out through the gap 111b, and the gas flow drives the wetting liquid J to flow together. Backflow, thereby reducing the wetting liquid J flowing out of the gas outlet 10b with the gas.
在一些示例中,相邻阻隔板111沿竖直方向X的投影相连,即相邻阻隔板111在水平面上的投影面连续设置或部分重叠。气体于间隙111b流动时,间隙内的气体整体会受到间隙111b两侧的阻隔板111的阻挡并改变流向,以此进一步减少随气体流出出气端10b的浸润液J。In some examples, the projections of adjacent barrier plates 111 along the vertical direction X are connected, that is, the projection surfaces of adjacent barrier plates 111 on the horizontal plane are arranged continuously or partially overlapped. When the gas flows in the gap 111b, the entire gas in the gap will be blocked by the barrier plates 111 on both sides of the gap 111b and change the flow direction, so as to further reduce the wetting liquid J flowing out of the gas outlet 10b with the gas.
在一些示例中,请参阅图2,阻隔板111包括多个阻隔部111a,多个阻隔部111a依次连接,相连的两个阻隔部111a之间具有夹角。气体流经第一阻隔机构11时,多个阻隔部111a可以多次的改变气体的流向,使气体所带动的浸润液依次被多个阻隔部111a所阻挡,可以进一步降低浸润液J流出出气端10b的流量。示例性地,阻隔板111可以包括两个或三个以上的阻隔部111a,随着阻隔部111a数量的增加,气体的流向被改变的次数增加,气体所带动的浸润液被更多的阻隔部111a所阻挡,能够更进一步减少随气体流出出气端10b的浸润液J。In some examples, please refer to FIG. 2 , the blocking plate 111 includes a plurality of blocking portions 111a, the plurality of blocking portions 111a are connected in sequence, and there is an included angle between two connected blocking portions 111a. When the gas flows through the first blocking mechanism 11, the multiple blocking parts 111a can change the flow direction of the gas multiple times, so that the wetting liquid driven by the gas is sequentially blocked by the multiple blocking parts 111a, which can further reduce the flow of the wetting liquid J out of the gas outlet. 10b traffic. Exemplarily, the barrier plate 111 may include two or more barrier parts 111a. As the number of barrier parts 111a increases, the number of times the flow direction of the gas is changed increases, and the immersion liquid carried by the gas is absorbed by more barrier parts. 111a can further reduce the wetting liquid J flowing out of the gas outlet 10b with the gas.
阻隔部111a可以沿水平方向延伸,随着延伸长度的增加,在水平方向上更多的浸润液J被阻挡回流。The blocking portion 111a may extend in the horizontal direction, and as the extension length increases, more immersion fluid J in the horizontal direction is blocked from flowing back.
请参阅图3和图4,阻隔板111可以直接或间接与第一管道10连接。例如,阻隔板111设置于第一管道10的管壁上。又例如,第一阻隔机构11还可以包括连接板112,连接板112沿竖直方向X延伸,连接板112包括沿水平方向相对设置的第一侧112a和第二侧112b,连接板112的第一侧112a和第一管道10的管壁连接,连接板112的第二侧112b上设置多个阻隔板111。通过将多个阻隔板111设置于连接板112上,便于将第一阻隔机构11从第一管道10上拆卸,方便更换和维修。Referring to FIG. 3 and FIG. 4 , the barrier plate 111 can be directly or indirectly connected to the first pipeline 10 . For example, the barrier plate 111 is disposed on the pipe wall of the first pipe 10 . As another example, the first blocking mechanism 11 may further include a connecting plate 112 extending along the vertical direction X, the connecting plate 112 includes a first side 112a and a second side 112b oppositely arranged along the horizontal direction, the second side of the connecting plate 112 One side 112 a is connected to the pipe wall of the first pipe 10 , and a plurality of barrier plates 111 are arranged on the second side 112 b of the connecting plate 112 . By arranging a plurality of blocking plates 111 on the connecting plate 112, it is convenient to disassemble the first blocking mechanism 11 from the first pipeline 10, which is convenient for replacement and maintenance.
在一些实施例中,请参阅图5,浸润腔10c内还设置有第二阻隔机构12,第二阻隔机构12连接于第一管道10的管壁,并位于第一阻隔机构11和进气端10a之间,第二阻隔机构12用于阻挡锂屑从出气端10b流出。锂屑经过浸润液J的惰化处理后,一部分锂屑可能会随着气体流动,而第二阻隔机构12可以起到阻挡锂屑的作用,能够减少经出气端10b流出的锂屑。In some embodiments, please refer to FIG. 5 , a second barrier mechanism 12 is also provided in the infiltration chamber 10c, and the second barrier mechanism 12 is connected to the tube wall of the first pipeline 10 and is located at the first barrier mechanism 11 and the inlet end. Between 10a, the second blocking mechanism 12 is used to block lithium chips from flowing out from the gas outlet 10b. After the lithium chips are inerted by the immersion solution J, part of the lithium chips may flow with the gas, and the second barrier mechanism 12 can block the lithium chips and reduce the lithium chips flowing out through the gas outlet 10b.
第二阻隔机构12可以设置于浸润液J内,锂屑的密度相比于浸润液J例如硅油的密度更小,锂屑随气体流经浸润腔10c时,锂屑受到浸润液J对锂屑竖直向上的浮力。为了进一步阻挡锂屑从出气端10b流出,第二阻隔机构12在水平面的截面积沿竖直方向逐渐增大或减小。锂屑由于受到浸润液J的浮力作用,锂屑能够平缓移动并聚积于第二阻隔机构12在竖直方向上的相对较高的部分,锂屑基本不会对第二阻隔机构12的相对较低的部分造成堵塞,气体和浸润液J可以从第二阻隔机构12的相对较低的部分流出。The second barrier mechanism 12 can be arranged in the immersion liquid J. The density of the lithium chips is lower than that of the immersion liquid J such as silicone oil. Vertical upward buoyancy. In order to further prevent lithium chips from flowing out from the gas outlet 10b, the cross-sectional area of the second blocking mechanism 12 on the horizontal plane increases or decreases gradually along the vertical direction. Due to the buoyancy effect of the immersion liquid J, the lithium chips can move smoothly and accumulate in the relatively high part of the second barrier mechanism 12 in the vertical direction, and the lithium chips will basically not affect the relatively high part of the second barrier mechanism 12. The lower portion causes blockage, and gas and immersion fluid J can flow out from the relatively lower portion of the second blocking mechanism 12 .
示例性地,请参阅图6和图7,第二阻隔机构12包括两个第一板121和两个第二板122。两个第二板122沿第二方向Z相对设置。两个第一板121沿第一方向Y相对设置,两个第一板121之间的间距沿竖直方向X向上逐渐增大,以使第二阻隔机构12在水平面的截面积沿竖直方向X逐渐增大。其中,两个第一板121之间的间距是指两个第一板121在第一方向Y上的间距。锂屑由于受到浸润液J的浮力作用,主要聚积于第一板121竖直方向X上相对较高的部分,第一板121和第二板122的相对较低的部分基本不会被锂屑堵塞,气体和浸润液J可以经第一板121和/或第二板122流出。Exemplarily, referring to FIG. 6 and FIG. 7 , the second blocking mechanism 12 includes two first plates 121 and two second plates 122 . The two second plates 122 are disposed opposite to each other along the second direction Z. As shown in FIG. The two first plates 121 are arranged opposite to each other along the first direction Y, and the distance between the two first plates 121 gradually increases upward along the vertical direction X, so that the cross-sectional area of the second blocking mechanism 12 on the horizontal plane is along the vertical direction X gradually increases. Wherein, the distance between the two first boards 121 refers to the distance between the two first boards 121 in the first direction Y. Due to the buoyancy of the immersion liquid J, lithium chips are mainly accumulated on the relatively high part of the first plate 121 in the vertical direction X, and the relatively low parts of the first plate 121 and the second plate 122 are basically not covered by lithium chips. Blockage, gas and immersion fluid J can flow out through the first plate 121 and/or the second plate 122 .
第一方向Y和第二方向Z均与水平面平行。第一管道10为方形管道时,第一方向Y为第一管道10的宽度方向,第二方向Z为第一管道10的长度方向。第一管道10为圆形管道时,第一方向Y和第二方向Z均为第一管道10的径向,并且第一方向 Y和第二方向Z垂直。Both the first direction Y and the second direction Z are parallel to the horizontal plane. When the first pipe 10 is a square pipe, the first direction Y is the width direction of the first pipe 10 , and the second direction Z is the length direction of the first pipe 10 . When the first pipe 10 is a circular pipe, the first direction Y and the second direction Z are both radial directions of the first pipe 10, and the first direction Y and the second direction Z are perpendicular.
第二阻隔机构12可以为中空结构体。例如,两个第一板121和两个第二板122连接并围合形成空腔12a,可以减轻设备的整体重量,以使设备轻量化,而且锂屑主要聚积于第一板121外,便于后续对锂屑的收集处理。为了便于气体和浸润液J流出,可以于第二阻隔机构12上开设通孔12b。示例性地,第一板121设置通孔12b,以便于气体流出至出气端10b。锂屑主要聚积于第一板121在竖直方向X上较高的部分。或者,第二板122上设置通孔12b,锂屑主要聚集于第一板121上,基本不会对第二板122造成堵塞,气体和浸润液J由第二板122的通孔12b流出。又或者,第一板121和第二板122均可以设置通孔12b,以增加气体和浸润液J的通过量,提高锂屑浸润惰化的处理效率。The second blocking mechanism 12 may be a hollow structure. For example, two first plates 121 and two second plates 122 are connected and enclosed to form a cavity 12a, which can reduce the overall weight of the equipment, so that the equipment is lightweight, and lithium chips are mainly accumulated outside the first plate 121, which is convenient Subsequent collection and treatment of lithium shavings. In order to facilitate the outflow of gas and immersion liquid J, a through hole 12 b may be opened on the second barrier mechanism 12 . Exemplarily, the first plate 121 is provided with a through hole 12b, so that the gas flows out to the gas outlet 10b. Lithium shavings are mainly accumulated on the higher part of the first plate 121 in the vertical direction X. Alternatively, the second plate 122 is provided with a through hole 12b, and the lithium chips mainly gather on the first plate 121, which basically does not cause blockage to the second plate 122, and gas and immersion liquid J flow out through the through hole 12b of the second plate 122. Alternatively, both the first plate 121 and the second plate 122 may be provided with through holes 12b to increase the throughput of gas and immersion liquid J and improve the treatment efficiency of infiltration and inertization of lithium shavings.
在一些实施例中,请参阅图8,浸润腔10c内还设置有过滤机构13,过滤机构13位于第一阻隔机构11和出气端10b之间,过滤机构13用于过滤气体中的锂屑和浸润液J。气体流经第一阻隔机构11后,仍可能会携带部分锂屑和浸润液J,经过过滤机构13的过滤作用,可以进一步减少流出出气端10b的锂屑和浸润液J。为了提高过滤机构13的过滤效果,过滤机构13可以包括多个过滤件。In some embodiments, please refer to FIG. 8 , a filter mechanism 13 is also provided in the infiltration chamber 10c, and the filter mechanism 13 is located between the first blocking mechanism 11 and the gas outlet 10b, and the filter mechanism 13 is used to filter lithium debris and Infiltrate J. After the gas flows through the first barrier mechanism 11, it may still carry some lithium chips and wetting solution J, and the filtering mechanism 13 can further reduce the lithium chips and wetting solution J flowing out of the gas outlet 10b. In order to improve the filtering effect of the filter mechanism 13, the filter mechanism 13 may include a plurality of filter elements.
示例性地,请参阅图8至图11,过滤机构13包括第二过滤件131和第三过滤件132,第二过滤件131靠近第一阻隔机构11设置,第三过滤件132位于第二过滤件131背离第一阻隔机构11的一侧。第二过滤件131可以用于过滤分离气体和锂屑。第三过滤件132可以用于过滤分离气体和浸润液J。Exemplarily, referring to FIG. 8 to FIG. 11 , the filter mechanism 13 includes a second filter element 131 and a third filter element 132, the second filter element 131 is arranged close to the first blocking mechanism 11, and the third filter element 132 is located at the second filter element 132. The side of the piece 131 facing away from the first blocking mechanism 11 . The second filter element 131 can be used to filter separated gas and lithium debris. The third filter element 132 can be used to filter the separation gas and the immersion liquid J.
请参阅图9,第二过滤件131连接于第一管道10的管壁,第二过滤件131具有多个第一过滤孔131a,多个第一过滤孔131a间隔排布,例如阵列排布或不均匀排布,在此并不限定第一过滤孔131a的排布方式。锂屑经过第二阻隔机构12的阻挡后,一部分锂屑可能会随着气体继续流动,通过对第一过滤孔131a的孔径进行调节,例如第一过滤孔131a的孔径小于锂屑的粒径,锂屑能够被第一过滤孔131a所阻挡,气体能够经第一过滤孔131a流出。Please refer to Fig. 9, the second filter element 131 is connected to the pipe wall of the first pipeline 10, the second filter element 131 has a plurality of first filter holes 131a, and the plurality of first filter holes 131a are arranged at intervals, for example arranged in an array or The uneven arrangement does not limit the arrangement of the first filter holes 131a here. After the lithium scraps are blocked by the second blocking mechanism 12, a part of the lithium scraps may continue to flow with the gas. By adjusting the aperture of the first filter hole 131a, for example, the aperture of the first filter hole 131a is smaller than the particle diameter of the lithium scraps. The lithium debris can be blocked by the first filter hole 131a, and the gas can flow out through the first filter hole 131a.
请参阅图10和图11,第三过滤件132可以包括多层过滤网,多层过滤网沿竖直方向X依次层叠设置,过滤网包括第二过滤孔132a。浸润液J经第一阻隔机构11的阻隔后,一部分浸润液J可能会随着气体继续流动,而第三过滤件132能够起到过滤分离气体和浸润液J的作用,气体和浸润液J通过多层过滤网被过滤分离,浸润液J被多层过滤网阻挡,气体经多层过滤网流出至第一管道10的出气端10b。如果经第二过滤件131过滤后,气体中仍携带有锂屑,在此情况下,气体和锂屑将会被多层过滤网过滤分离,以进一步净化气体。Please refer to FIG. 10 and FIG. 11 , the third filter element 132 may include a multi-layer filter net, and the multi-layer filter net is stacked in sequence along the vertical direction X, and the filter net includes a second filter hole 132a. After the immersion liquid J is blocked by the first blocking mechanism 11, a part of the immersion liquid J may continue to flow with the gas, while the third filter element 132 can filter and separate the gas and the immersion liquid J, and the gas and the immersion liquid J pass through The multi-layer filter is filtered and separated, the infiltration liquid J is blocked by the multi-layer filter, and the gas flows out to the gas outlet end 10b of the first pipeline 10 through the multi-layer filter. If after being filtered by the second filter element 131 , the gas still carries lithium shavings, in this case, the gas and lithium shavings will be filtered and separated by a multi-layer filter to further purify the gas.
为了更进一步净化气体,相邻过滤网的第二过滤孔132a可以错位排布,浸润液J和锂屑将会进一步被阻挡,从而更进一步提高气体的净化率。In order to further purify the gas, the second filter holes 132a of adjacent filter screens can be arranged in a dislocation, and the immersion liquid J and lithium chips will be further blocked, thereby further improving the gas purification rate.
在一些实施例中,请参阅图12,为了将惰化后的锂屑进行收集,锂屑惰化处理装置还包括第二管道20和收集机构21。第二管道20和第一管道10连接,第二管道20包括进液端20a和出液端20b,进液端20a和浸润腔10c连接。收集机构21连接于第二管道20的管壁,收集机构21用于分离浸润液J和锂屑。锂屑经第一管道10的浸 润腔10c内的浸润液J浸润惰化后,将浸润液J引流至第二管道20的收集机构21内,浸润液J将带动锂屑流动至收集机构21内,浸润液J和锂屑能够在收集机构21内被过滤分离,锂屑留存至收集机构21内,浸润液J流出收集机构21,达到对锂屑收集的目的。In some embodiments, referring to FIG. 12 , in order to collect the inerted lithium chips, the device for inerting lithium chips further includes a second pipeline 20 and a collection mechanism 21 . The second pipeline 20 is connected to the first pipeline 10, the second pipeline 20 includes a liquid inlet 20a and a liquid outlet 20b, and the liquid inlet 20a is connected to the infiltration chamber 10c. The collection mechanism 21 is connected to the pipe wall of the second pipeline 20, and the collection mechanism 21 is used for separating the immersion liquid J and lithium chips. After the lithium chips are infiltrated and inerted by the infiltration solution J in the infiltration cavity 10c of the first pipeline 10, the infiltration solution J is drained into the collection mechanism 21 of the second pipeline 20, and the infiltration solution J will drive the lithium chips to flow into the collection mechanism 21 , The infiltration solution J and the lithium chips can be filtered and separated in the collection mechanism 21, the lithium chips are retained in the collection mechanism 21, and the infiltration solution J flows out of the collection mechanism 21 to achieve the purpose of collecting lithium chips.
为了将浸润液J和锂屑过滤分离,收集机构21包括收集腔211和第一过滤件212,第一过滤件212设置于收集腔211。第一过滤件212可以将锂屑截留至收集机构21内,浸润液J通过第一过滤件212流出。示例性地,第二管道20为圆形管道,收集机构21围绕第二管道20的轴向形成收集腔211。In order to filter and separate the immersion liquid J from lithium debris, the collection mechanism 21 includes a collection chamber 211 and a first filter element 212 , and the first filter element 212 is disposed in the collection chamber 211 . The first filter element 212 can trap lithium debris into the collection mechanism 21 , and the infiltration liquid J flows out through the first filter element 212 . Exemplarily, the second pipe 20 is a circular pipe, and the collection mechanism 21 forms a collection cavity 211 around the axial direction of the second pipe 20 .
收集机构21和第二管道20之间的连接方式具有多种形式,示例性地,收集机构21和第二管道20之间可采用可拆卸方式连接,便于取出锂屑、更换收集机构21。当然,收集机构21和第二管道20之间也可固定连接,装置整体的结构稳定性更好。The connection between the collection mechanism 21 and the second pipeline 20 has various forms. For example, the collection mechanism 21 and the second pipeline 20 can be connected in a detachable manner, which is convenient for removing lithium chips and replacing the collection mechanism 21 . Of course, the collection mechanism 21 and the second pipeline 20 can also be fixedly connected, so that the overall structural stability of the device is better.
本申请实施例可以根据生产状况灵活设置第一管道10和第二管道20的相对位置。示例性地,第二管道20在竖直方向X上可以位于第一管道10的下方,利用浸润液J和锂屑自身的重力作用,浸润液J和锂屑可以从第一管道10流至第二管道20内,不需额外设置其他引流设备,可以简化装置的结构。In the embodiment of the present application, the relative positions of the first pipeline 10 and the second pipeline 20 can be flexibly set according to production conditions. Exemplarily, the second pipe 20 can be located below the first pipe 10 in the vertical direction X, and the immersion liquid J and lithium chips can flow from the first pipe 10 to the second pipe 10 by using the gravity of the immersion liquid J and lithium chips themselves. In the second pipeline 20, there is no need to additionally arrange other drainage equipment, which can simplify the structure of the device.
请参阅图12,为了分别调节第一管道10和第二管道20的生产节奏,可以于第二管道20内设置第一开关22,第一开关22位于收集机构21和进液端20a之间,第一开关22被配置为控制收集机构21与浸润腔10c的通断。气体在进入第一管道10时,第一开关22控制收集机构21与浸润腔10c断开,气体带动锂屑流动,锂屑在第一管道10的浸润腔10c内被浸润液J浸润惰化。当锂屑在第一管道10内被浸润惰化后,第一开关22控制收集机构21与浸润腔10c连通,浸润液J流至第二管道20内,浸润液J带动锂屑流动,浸润液J和锂屑被第二管道20的收集机构21过滤分离。浸润液J和锂屑经第二管道20的收集机构21过滤分离后,可以将净化后的浸润液J进一步循环利用。Referring to Fig. 12, in order to adjust the production rhythm of the first pipeline 10 and the second pipeline 20 respectively, a first switch 22 can be set in the second pipeline 20, and the first switch 22 is located between the collecting mechanism 21 and the liquid inlet 20a, The first switch 22 is configured to control the connection between the collection mechanism 21 and the infiltration chamber 10c. When the gas enters the first pipeline 10, the first switch 22 controls the collection mechanism 21 to disconnect from the infiltration chamber 10c, the gas drives the flow of lithium chips, and the lithium chips are infiltrated and inerted by the infiltration solution J in the infiltration chamber 10c of the first pipeline 10. After the lithium chips are infiltrated and inerted in the first pipeline 10, the first switch 22 controls the collection mechanism 21 to communicate with the infiltration chamber 10c, and the infiltration solution J flows into the second pipeline 20, and the infiltration solution J drives the lithium chips to flow, and the infiltration solution J flows into the second pipeline 20. J and lithium shavings are filtered and separated by the collection mechanism 21 of the second pipeline 20 . After the immersion solution J and lithium chips are filtered and separated by the collection mechanism 21 of the second pipeline 20, the purified immersion solution J can be further recycled.
在一些实施例中,请参阅图12,锂屑惰化处理装置1还包括第三管道30,第三管道30包括第一端30a和第二端30b,第一端30a与第二管道20的出液端20b连接,第二端30b与浸润腔10c连接,第三管道30用于将收集机构21分离出的浸润液J输送到浸润腔10c。浸润液J经第二管道20的收集机构21净化后,第三管道30将净化后的浸润液J循环至浸润腔10c,以此提高浸润液J的利用率。可以于第一端30a和第二端30b之间设置吸液泵31,利用吸液泵31将净化后的浸润液J循环。In some embodiments, please refer to FIG. 12 , the lithium scrap inerting treatment device 1 further includes a third pipeline 30, the third pipeline 30 includes a first end 30a and a second end 30b, the first end 30a and the second pipeline 20 The outlet end 20b is connected, the second end 30b is connected to the infiltration chamber 10c, and the third pipe 30 is used to transport the infiltration liquid J separated by the collection mechanism 21 to the infiltration chamber 10c. After the wetting fluid J is purified by the collecting mechanism 21 of the second pipeline 20, the third pipeline 30 circulates the purified wetting fluid J to the infiltration chamber 10c, thereby improving the utilization rate of the wetting fluid J. A liquid suction pump 31 may be provided between the first end 30a and the second end 30b, and the purified infiltration liquid J is circulated by the liquid suction pump 31 .
可选地,第二端30b位于出气端10b和第一阻隔机构11之间。净化后的浸润液J流经第一阻隔机构11时,可以将粘附于第一阻隔机构11的锂屑冲击至浸润液J中,避免锂屑堵塞第一阻隔机构11,使气体能够顺畅排出。Optionally, the second end 30b is located between the gas outlet end 10b and the first blocking mechanism 11 . When the purified immersion solution J flows through the first barrier mechanism 11, it can impact the lithium chips adhering to the first barrier mechanism 11 into the immersion solution J, preventing the lithium chips from clogging the first barrier mechanism 11, so that the gas can be discharged smoothly .
可选地,第二端30b位于出气端10b和第二过滤件131之间。净化后的浸润液J流经第二过滤件131时,可将粘附于第二过滤件131的锂屑冲击至浸润液J中,避免锂屑堵塞第二过滤件131和第一阻隔机构11,使气体能够顺畅排出。Optionally, the second end 30b is located between the gas outlet end 10b and the second filter element 131 . When the purified immersion liquid J flows through the second filter element 131, the lithium chips adhering to the second filter element 131 can be impacted into the immersion liquid J, so as to prevent the lithium chips from clogging the second filter element 131 and the first blocking mechanism 11 , so that the gas can be discharged smoothly.
本申请实施例还提供了一种锂屑惰化处理方法,请参阅图13,该方法包括:The embodiment of the present application also provides a lithium scrap inerting treatment method, please refer to Figure 13, the method includes:
S100,提供第一管道和第一阻隔机构,第一管道包括进气端、浸润腔、出气端 和位于进气端和出气端之间的浸润腔,浸润腔内容纳有浸润液,第一阻隔机构设置于浸润腔内;S100, providing a first pipeline and a first barrier mechanism, the first pipeline includes an inlet end, an infiltration chamber, an outlet end, and an infiltration chamber between the inlet end and the outlet end, the infiltration chamber contains an infiltration liquid, and the first barrier The mechanism is set in the infiltration chamber;
S200,将引流系统与出气端连接,并利用引流系统带动包含锂屑的气体流过第一管道,气体流经浸润腔时浸润锂屑,其中,S200, connecting the drainage system with the gas outlet, and using the drainage system to drive the gas containing lithium chips to flow through the first pipeline, and infiltrate the lithium chips when the gas flows through the infiltration chamber, wherein,
在气体流过第一管道时,第一阻隔机构阻挡至少部分浸润液从出气端流出。When the gas flows through the first pipe, the first blocking mechanism blocks at least part of the wetting liquid from flowing out from the gas outlet.
请参阅图14至图17,本申请实施例的锂屑惰化处理1的流程如下:Please refer to Fig. 14 to Fig. 17, the process flow of lithium scrap inerting treatment 1 in the embodiment of the present application is as follows:
请参阅图14,第一开关22控制浸润腔10c和第二管道20的收集机构21断开。气体经引流系统引流至浸润腔10c内的浸润液J内,气体带动锂屑和浸润液流动,锂屑流经第二阻隔机构12时被阻挡,并于浸润液J中被浸润惰化。同时,浸润液J经第一阻隔机构11阻挡回流,气体继续流至过滤机构13,经过滤机构13过滤净化并流出第一管道10的出气端10b。Referring to FIG. 14 , the first switch 22 controls the infiltration chamber 10 c and the collection mechanism 21 of the second pipeline 20 to be disconnected. The gas is drained into the infiltration solution J in the infiltration chamber 10c through the drainage system, and the gas drives the lithium chips and the infiltration solution to flow. When the lithium chips flow through the second blocking mechanism 12, they are blocked and infiltrated and inerted in the infiltration solution J. At the same time, the immersion liquid J passes through the first blocking mechanism 11 to block backflow, and the gas continues to flow to the filter mechanism 13 , where it is filtered and purified by the filter mechanism 13 and flows out of the gas outlet 10 b of the first pipeline 10 .
请参阅图15,第一开关22控制浸润腔10c和第二管道20的收集机构21连通,浸润液J流动并带动锂屑流至第二管道20的收集机构21内,浸润液J经收集机构21过滤净化。Please refer to Fig. 15, the first switch 22 controls the communication between the infiltration chamber 10c and the collection mechanism 21 of the second pipeline 20, the infiltration solution J flows and drives the lithium chips to flow into the collection mechanism 21 of the second pipeline 20, and the infiltration solution J passes through the collection mechanism 21 filter purification.
请参阅图16,第一开关22控制浸润腔10c和第二管道20的收集机构21断开,净化后的浸润液J经第三管道30循环至过滤机构13的第二过滤件131和第三过滤件132之间,浸润液J回流至浸润腔10c内。Please refer to Fig. 16, the first switch 22 controls the disconnection of the collection mechanism 21 of the infiltration chamber 10c and the second pipeline 20, and the purified infiltration liquid J circulates to the second filter element 131 and the third filter element 13 of the filter mechanism 13 through the third pipeline 30. Between the filter elements 132, the infiltration liquid J flows back into the infiltration chamber 10c.
请参阅图17,第二管道20内的浸润液J回流至第一管道10的浸润腔10c内,收集机构21内截留锂屑。Please refer to FIG. 17 , the wetting liquid J in the second pipeline 20 flows back into the wetting cavity 10 c of the first pipeline 10 , and lithium chips are trapped in the collection mechanism 21 .
本申请实施例还提供了一种电池补锂系统,请参阅图18,该电池补锂系统100,包括补锂装置2和本申请上述任一实施例的锂屑惰化处理装置1,锂屑惰化处理装置1的进气端与补锂装置2相对设置。补锂装置用于对电池的极片进行补锂,在补锂的过程中,可能会产生锂屑;锂屑惰化处理装置1的进气端与补锂装置2相对设置,以在补锂的过程中将锂屑抽入到锂屑惰化处理装置1的浸润腔内,锂屑在浸润液中被浸润,锂屑的表面被浸润液包裹惰化,可防止锂屑发生自燃等现象,进而提高电池生产的安全性。The embodiment of the present application also provides a battery lithium supplement system, please refer to FIG. 18, the battery lithium supplement system 100 includes a lithium supplement device 2 and the lithium scrap inerting treatment device 1 of any of the above-mentioned embodiments of the present application, and the lithium scrap The intake end of the inerting treatment device 1 is set opposite to the lithium replenishment device 2 . The lithium replenishment device is used to replenish lithium to the pole piece of the battery. During the lithium replenishment process, lithium scraps may be generated; During the process, the lithium chips are pumped into the infiltration cavity of the lithium chip inerting treatment device 1, the lithium chips are infiltrated in the immersion liquid, and the surface of the lithium chips is wrapped and inerted by the immersion liquid, which can prevent the spontaneous combustion of the lithium chips, etc. Thus improving the safety of battery production.
虽然已经参考优选实施例对本申请进行了描述,但在不脱离本申请的范围的情况下,可以对其进行各种改进并且可以用等效物替换其中的部件,尤其是,只要不存在结构冲突,各个实施例中所提到的各项技术特征均可以任意方式组合起来。本申请并不局限于文中公开的特定实施例,而是包括落入权利要求的范围内的所有技术方案。While the application has been described with reference to a preferred embodiment, various modifications may be made thereto and equivalents may be substituted for parts thereof without departing from the scope of the application, in particular, as long as there are no structural conflicts , the technical features mentioned in each embodiment can be combined in any way. The present application is not limited to the specific embodiments disclosed herein, but includes all technical solutions falling within the scope of the claims.

Claims (17)

  1. 一种锂屑惰化处理装置,包括:A lithium scrap inerting treatment device, comprising:
    第一管道,包括进气端、出气端和位于所述进气端和所述出气端之间的浸润腔,所述出气端用于与外部的引流系统连接,所述引流系统用于带动包含锂屑的气体流过所述第一管道,所述浸润腔用于容纳浸润液,以在所述气体流经所述浸润腔时浸润所述锂屑;以及The first pipeline includes an air inlet end, an air outlet end, and an infiltration chamber between the air inlet end and the air outlet end. The air outlet end is used to connect with an external drainage system, and the drainage system is used to drive the A gas of lithium chips flows through the first pipeline, and the wetting chamber is configured to contain an infiltration liquid to wet the lithium chips as the gas flows through the wetting chamber; and
    第一阻隔机构,设置于所述浸润腔内,并用于在所述气体流过所述第一管道时阻挡至少部分所述浸润液从所述出气端流出。The first blocking mechanism is arranged in the wetting chamber, and is used for blocking at least part of the wetting liquid from flowing out from the gas outlet when the gas flows through the first pipeline.
  2. 根据权利要求1所述的锂屑惰化处理装置,其中,所述进气端位于所述出气端竖直方向的上方,所述第一阻隔机构包括多个间隔设置的阻隔板,相邻的所述阻隔板之间形成供所述气体流过的间隙,所述阻隔板的至少部分相对于所述竖直方向倾斜。The lithium scrap inerting treatment device according to claim 1, wherein the inlet end is located above the outlet end in the vertical direction, and the first blocking mechanism includes a plurality of blocking plates arranged at intervals, adjacent A gap for the gas to flow is formed between the barrier plates, and at least part of the barrier plates are inclined relative to the vertical direction.
  3. 根据权利要求2所述的锂屑惰化处理装置,其中,所述阻隔板包括多个所述阻隔部,多个所述阻隔部依次连接,相连的两个所述阻隔部之间具有夹角。The lithium scrap inerting treatment device according to claim 2, wherein the barrier plate includes a plurality of barrier parts, and the plurality of barrier parts are connected in sequence, and there is an included angle between two connected barrier parts. .
  4. 根据权利要求2或3所述的锂屑惰化处理装置,其中,相邻所述阻隔板沿所述竖直方向的投影相连。The lithium scrap inerting treatment device according to claim 2 or 3, wherein the projections of adjacent barrier plates along the vertical direction are connected.
  5. 根据权利要求1至4中任一项所述的锂屑惰化处理装置,其中,所述浸润腔内还设置有第二阻隔机构,所述第二阻隔机构连接于所述第一管道的管壁,并位于所述第一阻隔机构和所述进气端之间,所述第二阻隔机构用于阻挡所述锂屑从所述出气端流出。The lithium scrap inerting treatment device according to any one of claims 1 to 4, wherein a second blocking mechanism is further provided in the infiltration chamber, and the second blocking mechanism is connected to the pipe of the first pipeline. The wall is located between the first blocking mechanism and the gas inlet end, and the second blocking mechanism is used to prevent the lithium chips from flowing out from the gas outlet.
  6. 根据权利要求5所述的锂屑惰化处理装置,其中,The lithium scrap inerting treatment device according to claim 5, wherein,
    所述第二阻隔机构在水平面的截面积沿竖直方向逐渐增大或逐渐减小。The cross-sectional area of the second blocking mechanism on the horizontal plane increases or decreases gradually along the vertical direction.
  7. 根据权利要求6所述的锂屑惰化处理装置,其中,所述第二阻隔机构包括:The lithium scrap inerting treatment device according to claim 6, wherein the second blocking mechanism comprises:
    沿第一方向相对设置的两个第一板,两个所述第一板之间的间距沿所述竖直方向向上逐渐增大;以及two first plates oppositely arranged along the first direction, the distance between the two first plates gradually increases upward along the vertical direction; and
    沿第二方向相对设置的两个第二板,两个所述第一板和两个所述第二板连接并围合形成空腔,所述第一板和/或所述第二板设置有多个通孔,以使所述气体和所述浸润液流出,所述第一方向和所述第二方向均与水平面平行,所述第一方向和所述第二方向垂直。Two second plates oppositely arranged along the second direction, the two first plates and the two second plates are connected and enclosed to form a cavity, the first plates and/or the second plates are set There are a plurality of through holes for the gas and the immersion liquid to flow out, the first direction and the second direction are parallel to the horizontal plane, and the first direction and the second direction are perpendicular.
  8. 根据权利要求1至7中任一项所述的锂屑惰化处理装置,其中,所述浸润腔内还设置有过滤机构,所述过滤机构位于所述第一阻隔机构和所述出气端之间,并用于过滤所述气体中的所述锂屑和所述浸润液。The lithium scrap inerting treatment device according to any one of claims 1 to 7, wherein a filtering mechanism is further provided in the infiltration chamber, and the filtering mechanism is located between the first blocking mechanism and the gas outlet and used to filter the lithium chips and the immersion liquid in the gas.
  9. 根据权利要求1至8中任一项所述的锂屑惰化处理装置,所述锂屑惰化处理装置还包括:According to the lithium scrap inerting treatment device according to any one of claims 1 to 8, the lithium scrap inerting treatment device further comprises:
    第二管道,所述第二管道和所述第一管道连接,所述第二管道包括进液端和出液端,所述进液端和所述浸润腔连接;以及a second pipeline, the second pipeline is connected to the first pipeline, the second pipeline includes a liquid inlet and a liquid outlet, and the liquid inlet is connected to the infiltration chamber; and
    收集机构,所述收集机构连接于所述第二管道的管壁,所述收集机构用于分离所述浸润液和所述锂屑。A collection mechanism, the collection mechanism is connected to the pipe wall of the second pipeline, and the collection mechanism is used to separate the immersion liquid and the lithium chips.
  10. 根据权利要求9所述的锂屑惰化处理装置,其中,所述第二管道在竖直方向上位于所述第一管道的下方。The lithium scrap inerting treatment device according to claim 9, wherein the second pipeline is vertically located below the first pipeline.
  11. 根据权利要求9或10所述的锂屑惰化处理装置,其中,所述收集机构包括收集腔和第一过滤件,所述第一过滤件设置于所述收集腔,并用于分离所述浸润液和所述锂屑。The lithium scrap inerting treatment device according to claim 9 or 10, wherein the collection mechanism includes a collection chamber and a first filter element, the first filter element is arranged in the collection chamber and is used to separate the infiltrated liquid and the lithium chips.
  12. 根据权利要求9至11任一项所述的锂屑惰化处理装置,其中,所述第二管道内还设置有第一开关,所述第一开关位于所述收集机构和所述进液端之间,所述第一开关被配置为控制所述收集机构与所述浸润腔的通断。The lithium scrap inerting treatment device according to any one of claims 9 to 11, wherein a first switch is further arranged in the second pipeline, and the first switch is located at the collection mechanism and the liquid inlet end Between, the first switch is configured to control the connection between the collection mechanism and the infiltration chamber.
  13. 根据权利要求9至12中任一项所述的锂屑惰化处理装置,其中,所述收集机构可拆卸设置于所述第二管道内。The lithium scrap inerting treatment device according to any one of claims 9 to 12, wherein the collection mechanism is detachably arranged in the second pipeline.
  14. 根据权利要求9至13中任一项所述的锂屑惰化处理装置,所述锂屑惰化处理装置还包括第三管道,所述第三管道包括第一端和第二端,所述第一端与所述第二管道的出液端连接,所述第二端与所述浸润腔连接,所述第三管道用于将所述收集机构分离出的所述浸润液输送到所述浸润腔。According to the lithium scrap inerting treatment device according to any one of claims 9 to 13, the lithium scrap inerting treatment device further includes a third pipeline, the third pipeline includes a first end and a second end, the The first end is connected to the liquid outlet end of the second pipeline, the second end is connected to the infiltration chamber, and the third pipeline is used to transport the infiltration liquid separated by the collection mechanism to the infiltration cavity.
  15. 根据权利要求14所述的锂屑惰化处理装置,其中,所述第二端位于所述出气端和所述第一阻隔机构之间。The lithium scrap inerting treatment device according to claim 14, wherein the second end is located between the gas outlet end and the first blocking mechanism.
  16. 一种电池补锂系统,包括:A battery lithium supplement system, comprising:
    补锂装置;以及Lithium supplementation devices; and
    如权利要求1至15中任一项所述的锂屑惰化处理装置,所述锂屑惰化处理装置的进气端与所述补锂装置相对设置。The lithium scrap inerting treatment device according to any one of claims 1 to 15, wherein the air intake end of the lithium scrap inerting treatment device is arranged opposite to the lithium replenishing device.
  17. 一种锂屑惰化处理方法,包括:A method for inerting lithium shavings, comprising:
    提供第一管道和第一阻隔机构,所述第一管道包括进气端、出气端和位于所述进气端和所述出气端之间的浸润腔,所述浸润腔内容纳有浸润液,所述第一阻隔机构设置于所述浸润腔内;A first pipeline and a first barrier mechanism are provided, the first pipeline includes an air inlet end, an air outlet end, and an infiltration chamber located between the air inlet end and the air outlet end, the infiltration chamber contains an infiltration liquid, The first blocking mechanism is arranged in the infiltration chamber;
    将引流系统与所述出气端连接,并利用所述引流系统带动包含锂屑的气体流过所述第一管道,所述气体流经所述浸润腔时浸润所述锂屑,Connecting the drainage system to the gas outlet, and using the drainage system to drive the gas containing lithium chips to flow through the first pipeline, and the gas flows through the infiltration chamber to infiltrate the lithium chips,
    其中,在所述气体流过所述第一管道时,所述第一阻隔机构阻挡至少部分所述浸润液从所述出气端流出。Wherein, when the gas flows through the first pipeline, the first blocking mechanism blocks at least part of the wetting liquid from flowing out from the gas outlet.
PCT/CN2022/097791 2021-08-31 2022-06-09 Lithium chip inerting processing apparartus and processing method, and battery lithium supplementing system WO2023029636A1 (en)

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