WO2023003340A1 - 젤리-롤형 전극 조립체 및 이의 제조 방법 - Google Patents
젤리-롤형 전극 조립체 및 이의 제조 방법 Download PDFInfo
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- WO2023003340A1 WO2023003340A1 PCT/KR2022/010590 KR2022010590W WO2023003340A1 WO 2023003340 A1 WO2023003340 A1 WO 2023003340A1 KR 2022010590 W KR2022010590 W KR 2022010590W WO 2023003340 A1 WO2023003340 A1 WO 2023003340A1
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- Prior art keywords
- separator
- jelly
- surface roughness
- electrode assembly
- alumina
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Images
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
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- H01M10/04—Construction or manufacture in general
- H01M10/0431—Cells with wound or folded electrodes
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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- H01M10/04—Construction or manufacture in general
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- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/04—Construction or manufacture in general
- H01M10/0404—Machines for assembling batteries
- H01M10/0409—Machines for assembling batteries for cells with wound electrodes
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/058—Construction or manufacture
- H01M10/0587—Construction or manufacture of accumulators having only wound construction elements, i.e. wound positive electrodes, wound negative electrodes and wound separators
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/403—Manufacturing processes of separators, membranes or diaphragms
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
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- H01M50/417—Polyolefins
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- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
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- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
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- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
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- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
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- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Definitions
- the present invention relates to a jelly-roll type electrode assembly and a method for manufacturing the same, and more particularly, to a jelly-roll type electrode assembly with improved safety and high process yield and a method for manufacturing the same.
- a secondary battery capable of charging and discharging is a method for solving air pollution such as existing gasoline vehicles using fossil fuels, electric vehicles (EVs), hybrid electric vehicles (HEVs), plug-in hybrid electric vehicles ( P-HEV), etc., the need for development of secondary batteries is increasing.
- secondary batteries are classified into cylindrical batteries and prismatic batteries in which the electrode assembly is embedded in a cylindrical or prismatic metal can, and pouch-type batteries in which the electrode assembly is embedded in a pouch-type case made of an aluminum laminate sheet. .
- Secondary batteries are also classified according to the structure of an electrode assembly having a laminated structure of a positive electrode, a negative electrode, and a separator interposed between the positive electrode and the negative electrode.
- a jelly-roll type (wound type) electrode assembly having a structure in which long sheet-type positive and negative electrodes are wound with a separator interposed therebetween, a plurality of positive and negative electrodes cut in units of a predetermined size with a separator interposed therebetween and stacked (stacked) electrode assemblies sequentially stacked.
- a stack/folding type electrode assembly which is a mixture of the jelly-roll type and stack type, has been developed.
- the jelly-roll type electrode assembly is the easiest to manufacture and has a high energy density per weight.
- Separation membrane isolates two electrodes (anode/cathode) in a secondary battery to block electrical short-circuit caused by physical contact, and provides a passage through which ions can move between the two electrodes through an electrolyte solution supported in micropores so as to have ionic conductivity. It is a film material with the function of In the case of a secondary battery for an electric vehicle, unlike conventional small electronic devices, heat resistance characteristics are required to secure the safety of the battery even in an environment exposed to heat of about 150 ° C.
- polypropylene which has excellent thermal properties, has recently been used as a material for separators, and a ceramic coated SRS (safety reinforced separator) separator with improved heat resistance by coating ceramic particles and a polymer binder on one side or both sides of the separator has been developed. It is applied to secondary batteries.
- the problem to be solved by the present invention is to provide a jelly-roll type electrode assembly and a method for manufacturing the same with improved safety and high process yield.
- the separator includes a double-sided coating layer, and the coating layer includes a mixture of first alumina and second alumina, ,
- the surface roughness (Ra) of the separator may be 500 nm to 1 ⁇ m, and a particle diameter of the first alumina may be smaller than a particle diameter of the second alumina.
- the second alumina may be included in 16 to 40 parts by weight.
- the first alumina may be included in 60 to 84 parts by weight.
- the particle diameter of the first alumina may be 20 to 50 nm.
- the particle diameter of the second alumina may be 300 to 500 nm.
- the electrode assembly may be a double-sided SRS laminate in which a separator, an anode, a separator, and a cathode are sequentially stacked.
- the length of the core of the jelly roll-type electrode assembly may be about 10 cm to 12 cm, and the radius may be about 4 cm to 5 cm.
- a method for manufacturing a jelly-roll type electrode assembly includes providing a separator including a double-sided coating layer, calculating a difference in surface roughness between the separator and the winding core, and If the difference between the surface roughness values is less than the first value, the surface roughness of the winding core is adjusted using a first process, and when the difference between the surface roughness values of the separator and the winding core is greater than or equal to the first value, a second process is performed.
- the coating layer comprises first alumina and It includes a mixture of second alumina, the surface roughness (Ra) of the separator is 500 nm to 1 ⁇ m, and the particle diameter of the first alumina may be smaller than the particle diameter of the second alumina.
- the second alumina may be included in 16 to 40 parts by weight.
- the first alumina may be included in 60 to 84 parts by weight.
- the first value Rmax may be between 0.05s and 0.15s.
- the first process may be a sanding process.
- the second process may be a lapping process.
- the sheet-like laminate is wound by a rod-shaped winding core, the winding core includes a first part and a second part separated around a rotation axis, and one end of the sheet-like laminate is the first part and the second part. It is fixed by being inserted into the slit between the second parts, and the size of the slit may be greater than 0.8 mm.
- the sheet-like laminate is wound by a rod-shaped core, the surface roughness of the core is less than or equal to a second value, and the second value (Rmax) may be 0.15 s to 0.25 s.
- the step of calculating the difference between the surface roughness of the separator and the winding core may be performed again.
- the step of adjusting the surface roughness of the winding core is performed using a second process. It can be.
- the step of adjusting the surface roughness of the winding core is performed using a first process. and winding the sheet-type laminate including the electrode and the separator using the winding core having the controlled surface roughness may be performed.
- a battery cell according to another embodiment of the present invention includes the above-described jelly-roll type electrode assembly.
- the jelly-roll type electrode assembly and method for manufacturing the same of the present invention include a double-sided SRS separator, thereby improving heat resistance and safety, and controlling the surface roughness of the SRS separator and the winding core, thereby improving process yield.
- FIG. 1 is a perspective view showing a jelly-roll type electrode assembly according to an embodiment of the present invention.
- FIG. 2 is a flowchart of a method for manufacturing a jelly-roll type electrode assembly according to an embodiment of the present invention.
- FIG 3 is a side view of a winding core used in a jelly-roll type electrode assembly manufacturing method according to an embodiment of the present invention.
- FIG. 4 is a cross-sectional view of a winding core used in a jelly-roll type electrode assembly manufacturing method according to an embodiment of the present invention.
- planar it means when the corresponding part is viewed from above, and when it is referred to as “cross-section”, it means when the cross section of the corresponding part cut vertically is viewed from the side.
- FIG. 1 is a perspective view showing a jelly-roll type electrode assembly according to an embodiment of the present invention.
- the jelly-roll type electrode assembly 100 of this embodiment may include a positive electrode 110, a negative electrode 120, and a separator 130 interposed between the positive electrode 110 and the negative electrode 120.
- a separator 130, a positive electrode 110, a separator 130, and a negative electrode 120 are stacked in this order, and a jelly-roll type electrode assembly 100 is shown in which the positive electrode 110 is wound inside.
- the separator 130, the negative electrode 120, the separator 130, and the positive electrode 110 may be stacked in order so that the negative electrode 120 is located inside.
- the positive electrode 110, the separator 130, the negative electrode 120, and the separator 130 are stacked in this order, or the negative electrode 120, the separator 130, the positive electrode 110, and the separator 130 are stacked in that order. It is also possible to become As such, the electrodes 110 and 120 and the separator 130 are alternately stacked to form a sheet-like stack, and the sheet-like stack may be wound by a long rod-shaped core.
- the positive electrode 110 and the negative electrode 120 may be collectively referred to as electrodes 110 and 120 .
- the electrodes 110 and 120 may be obtained by applying a slurry containing an electrode active material on a current collector.
- the electrode slurry may typically include an electrode active material, a conductive material, a binder, and a solvent, but is not limited thereto.
- the current collector may be made of stainless steel, aluminum, copper, nickel, titanium, calcined carbon, or the like, and may be provided in various forms such as a film, sheet, foil, net, porous material, foam, or non-woven fabric.
- Examples of the current collector used for the positive electrode 110 include aluminum or an alloy thereof, and examples of the current collector used for the negative electrode 120 include copper, nickel, stainless steel, or any one of these alloys. .
- the separator 130 may separate the positive electrode 110 and the negative electrode 120 and provide a passage for ions moving between the positive electrode 110 and the negative electrode 120 .
- Separator 130 is a major component that determines the performance of a secondary battery.
- physical properties such as minimizing thickness to lower electrical resistance and maximizing porosity and pore size are required. must be satisfied
- electrochemical properties such as wettability with an electrolyte must also be satisfied.
- the separator 130 melts, causing an internal short circuit of the battery cell. Therefore, since the separator 130 used in the secondary battery must satisfy heat resistance in addition to physical and electrochemical properties, attempts have been made to change the material of the separator 130 to polyolefin, polyethylene, polypropylene, or a composite thereof. Recently, in addition to simply changing the material, a method of manufacturing a separator 130 in which one or both sides of a porous substrate such as polyolefin, polyethylene, or polypropylene is coated with a coating material of ceramic material is mainly used. Such a separator 130 may be referred to as an SRS or an SRS separator, and details of the SRS separator may be described with reference to known literature.
- a coating layer may be formed by applying a coating material to one side or both sides of the separation membrane 130 , and heat resistance and safety of the separation membrane 130 may be improved by the coating layer.
- a coating material including alumina (Al 3 O 2 ) and a binder may be coated on one side or both sides of the fabric of the separator 130 .
- the separator 130 physically continuously blocks contact between the positive electrode and the negative electrode even in a high-temperature situation inside the battery cell such as thermal runaway, thereby preventing an internal short circuit of the battery cell.
- the separator 130 may be provided as a double-sided SRS separator.
- a coating layer may be formed by applying a coating material to both surfaces of the fabric of the separator 130 facing the electrodes 110 and 120 .
- the coating layer is formed on both sides of the separation membrane 130, since either one side or the other side of the separation membrane 130 is in contact with the electrodes 110 and 120, the separation membrane 130 can be freely disposed in the process. In addition, simplification of the process and reduction of process time can be achieved accordingly.
- the coating layer of the separator 130 may include ceramic particles and a polymer binder.
- An example of the ceramic particle is alumina, and the characteristics of the separator 130 may vary depending on the diameter of the alumina. For example, as the diameter of alumina decreases, the surface area of the particles increases, and since a relatively large number of particles can contact the original fabric of the separation membrane 130, the adhesion of the particles is improved and deformation of the separation membrane 130 is suppressed. can In addition, even when the coating material is repeatedly applied on the fabric of the separator 130, the thickness of the coating layer can be reduced if the particle diameter is small, so the air permeability of the coating layer increases compared to the case where the particle diameter is large, The ion conduction resistance of (130) can be lowered. In order to achieve the above effect, fine particles of alumina having a small diameter may be used as a material for the coating material, and their diameter may be 20 to 50 nm.
- the coating layer of the separator 130 may be formed on both sides, and the surface roughness of the separator 130 may be determined by the coating layer.
- the surface roughness of the coating layer may be low, and accordingly, a phenomenon (slip phenomenon) of the separator 130 may appear during the winding process.
- the separator 130 may be cut or damaged during the winding process.
- the separation membrane 130 may be pulled out along the winding core or the separation membrane 130 may be damaged. Therefore, the surface roughness of the separator 130 applied to the jelly-roll electrode assembly 100 may need to be properly adjusted.
- the surface roughness of the separator 130 may be adjusted by adjusting the particle size of alumina included in the coating material.
- the coating material may include a mixture of fine particle alumina and general alumina. Since the surface roughness of the coating layer may vary depending on the ratio of fine alumina particles and normal alumina included in the mixture, a coating layer of an appropriate level required for the separator 130 may be formed by varying the ratio of the two particles. At this time, since the surface roughness of an appropriate level may vary depending on the difference in roughness with respect to the winding core, the width of the separator 130, or the size of the jelly-roll type electrode assembly, the appropriate mixture ratio may vary as each condition changes. there is. As will be described later, it may be desirable for the mixture to include normal alumina in a proportion of 40% or less. The mixture may preferably contain normal alumina in a proportion of at least 16%.
- normal alumina is for distinction from fine particle alumina, and may refer to alumina particles having a larger diameter than fine particle alumina.
- the diameter of normal alumina may be 300 to 500 nm.
- the fine particle alumina may be referred to as a first alumina, and the normal alumina may be referred to as a second alumina.
- the winding core may contact one end of the separator 130 extending from one end of the electrodes 110 and 120 in the winding process. . Therefore, when the difference in surface roughness between the separator 130 and the winding core is large, a problem may occur that a part of the separator 130 is pulled out or the separator 130 is damaged when the winding core is discharged, and thus the electrode assembly 100 The yield of may be lowered.
- the manufacturing method according to the present embodiment may include a process of adjusting the surface roughness of the winding core according to the difference in surface roughness between the separator 130 and the winding core.
- FIG. 2 is a flowchart of a method for manufacturing a jelly-roll type electrode assembly according to an embodiment of the present invention.
- 3 is a side view of a winding core used in a jelly-roll type electrode assembly manufacturing method according to an embodiment of the present invention.
- 4 is a cross-sectional view of a winding core used in a jelly-roll type electrode assembly manufacturing method according to an embodiment of the present invention.
- the manufacturing method (S1000) of the electrode assembly 100 according to this embodiment is the manufacturing method (S1000) of the electrode assembly 100 according to this embodiment.
- Preparing a separator (S1100), comparing the surface roughness values of the separator and the winding core (S1200), adjusting the surface roughness of the winding core based on the compared value (S1300), and using the winding core to separate the separator and the electrode It may include a step (S1400) of winding a sheet-like laminate comprising a.
- the core 200 may have a long rod shape.
- a cross section of the winding core 200 may have a circular shape as a whole.
- One end of the winding core 200 may be separated based on a central axis, and cross sections of the separated parts may each have a semicircular shape.
- the separated parts may be referred to as a first part 210a and a second part 210b, respectively.
- a sheet-like laminate may be inserted between the first part 210a and the second part 210b facing each other in the winding core 200, and the sheet-like laminate is formed on the outer surface of the winding core 200 ( 220) can be wound along.
- the sheet-like laminate can be wound in a jelly-roll shape.
- the winding core 200 may be positioned on the core 100a.
- the core 200 positioned on the core 100a may be removed from the jelly-roll type electrode assembly 100 .
- the winding core 200 may not be discharged due to frictional force between the winding core 200 and the separator 130 located in the innermost layer of the electrode assembly 100.
- the separator 130 is damaged due to the frictional force between the separator 130 and the winding core 200, or a defect in which the separator 130 is pulled out of the electrode assembly 100 may occur, resulting in a decrease in production efficiency and electrode Disconnection of (110, 120) and internal short-circuit may cause problems that deteriorate the safety of the secondary battery. Therefore, in order to minimize this phenomenon, a flat portion 230 extending in the longitudinal direction may be formed on a portion of the outer surface 220 of the winding core 200 .
- the length t1 of the flat portion 230 may correspond to the length of the sheet-like laminate, specifically, the length of the core 100a.
- a distance between the first portion 210a and the second portion 210b into which the sheet-like laminate is inserted may be greater than the thickness of the sheet-like laminate. If the distance between the first part 210a and the second part 210b is similar to the thickness of the sheet-like laminate, the winding core 200 and the sheet-like laminate can be well fixed, but in the process of removing the winding core 200 A part of the sheet-like laminate may be damaged.
- the separation space between the first part 210a and the second part 210b, that is, the size g1 of the slit is fixed between the winding core 200 and the sheet-like laminate, but the contact between the winding core 200 and the sheet-like laminate needs to be designed to a level that is minimized.
- the size (g1) of the conventional slit is designed to be around 0.8 mm, but in this embodiment to which the double-sided SRS separator is applied, the size (g1) of the slit may be preferably 0.8 mm or more. It may be preferable that the size g1 of the slit in this embodiment be designed at a level of 0.8 to 1.2 mm.
- the separator 130 may be provided as a double-sided SRS separator (S1100).
- a coating layer may be formed by applying a coating material to both sides of the separator 130 .
- the coating material may include ceramic particles and a polymer binder.
- the ceramic particles may include first alumina and second alumina, and a ratio of the second alumina may be within 40%.
- Provision of the separation membrane 130" described in the step (S1100) can be interpreted as including both manufacturing the separation membrane 130 or putting the manufactured separation membrane 130 into this manufacturing process.
- the provided separator 130 may be alternately stacked with the positive electrode 110 and the negative electrode 120 to form a sheet-like laminate.
- the sheet-like stacked body may be manufactured into a jelly-roll type electrode assembly 100 by being wound by a winding core 200 .
- the manufacturing process of the present embodiment may include calculating a difference in surface roughness between the separator 130 and the winding core 200 .
- the surface roughness of the winding core 200 may mean the surface roughness of the outer surface 220 .
- the surface roughness of the separator 130 and the winding core 200 is compared, and a difference between the two values can be calculated (S1200).
- the comparison of the surface roughness and the calculation of the difference value may be performed by a controller or a server of a device performing the present manufacturing method.
- the surface roughness of the separator 130 and the winding core 200 may be measured or obtained from a supplier of the separator 130 or the winding core 200 .
- the surface roughness may be measured by a non-contact type or a contact type roughness meter, and for example, it may be measured by a Mitutoyo SJ-410 roughness meter.
- the control unit or server may compare the measured or acquired surface roughness values and calculate a difference value.
- the surface roughness of the winding core 200 may be adjusted (S1300).
- the surface roughness of the workpiece that is, the frictional force
- prevention of frictional resistance according to the contact area prevention of grooves due to surface roughness
- prevention of grooves due to differences in hardness prevention of adhesion through surface treatment
- a polishing process such as sand blasting or lapping to minimize frictional resistance and prevent grooves by polishing the surface may be appropriate.
- a surface treatment method such as DLC (Diamond Like Carbon) or CrN (Chrome Nitrate), which prevents adhesion by coating the surface, may be applied.
- DLC Diamond Like Carbon
- CrN Chrome Nitrate
- Table 1 below shows the degree of finishing in the sanding process and lapping process
- Table 2 shows the processing level according to the finishing symbol.
- Rmax may mean the maximum height of surface roughness
- Rz may mean average roughness of 10 points
- Ra may mean average roughness of the center line.
- the sanding process may be a process of polishing the surface of a workpiece by spraying fine particles of various materials onto the surface of the workpiece using high-pressure air or a high-speed rotating impeller. Uniform irregularities may be formed on the surface of the workpiece by the sanding process, and foreign matter remaining on the surface after processing may be removed.
- the size of the particles used in the sanding process may be 120 to 150 mesh. 150mesh may mean a level of 106um.
- the lapping process may be a precision machining method of finishing a workpiece by abrasion and grinding action using a tool called a lap and a lap agent.
- the protrusions on the surface of the workpiece are removed by applying appropriate pressure to the wrapper against the workpiece, thereby improving surface precision and increasing the degree of contact between the contact surfaces.
- the surface roughness may be 0.15 s to 0.25 s (Rmax), preferably 0.2 s (Rmax). Since the surface roughness of the winding core 200 is improved through the lapping process, damage to the separator 130 that may occur when the winding core 200 is removed can be prevented.
- the polishing level of the lapping process is higher than that of the sanding process. Accordingly, when a difference in surface roughness between the winding core 200 and the separator 130 is large based on a specific reference value, a lapping process may be applied to improve the surface roughness of the winding core 200 . When the difference in surface roughness is not large, a sanding process may be applied to improve the surface roughness of the winding core 200 .
- a difference in surface roughness between the winding core 200 and the separator 130 may be compared based on a predetermined value. If the difference in surface roughness is less than a predetermined value, the surface roughness of the winding core 200 and the separator 130 is similar.
- the first process is applied. and applying a second process if the value is greater than or equal to the first value.
- the first value may be 0.05s to 0.15s (Rmax), preferably 0.1s (Rmax).
- the first process may be a sanding process, and the second process may be a lapping process.
- the manufacturing method of this embodiment may proceed to the step of winding the sheet-like laminate (S1400) after the above-described step of adjusting the surface roughness (S1300), but the surface roughness of the winding core 200 and the separator 130 Steps (S1200) and (S1300) may be repeatedly performed until the difference is less than the first value. This may be done so that the frictional force between the winding core 200 and the separator 130 is formed at a desired level by making the difference in surface roughness between the winding core 200 and the separator 130 less than or equal to the first value.
- the desired surface roughness of the winding core 200 may be 0.15 s to 0.25 s (Rmax), preferably 0.2 s (Rmax).
- step S1200 when the surface roughness difference between the winding core 200 and the separator 130 calculated through step S1200 is greater than the first value, a lapping process may be applied to the winding core 200 through step S1300. Thereafter, the manufacturing method according to the present embodiment proceeds to step (S1200) again, and the surface roughness of the winding core 200 to which the lapping process is applied may be measured. Through step (S1200), the surface roughness value of the winding core 200 after the wrapping process is completed is confirmed, and the difference between the surface roughness of the winding core 200 and the surface roughness of the separator 130 after the wrapping process is completed can be calculated again. .
- step S1400 the lapping process may be applied to the core 200 through step S1300, and step S1200 may be repeated again. If the calculated difference value is less than the first value, a sanding process may be applied to the winding core 200 through step S1300. Thereafter, the manufacturing method according to the present embodiment may proceed to step (S1400).
- a sheet-like laminate including a separator and an electrode may be wound using the winding core 200 (S1400).
- one end of the core 200 may include a first part 210a and a second part 210b cut with respect to the central axis.
- the size g1 of the slit is fixed between the winding core 200 and the sheet-type laminate, but needs to be designed to minimize contact between the winding core 200 and the sheet-type laminate. At this time, it may be preferable to design the size g1 of the slit to be 0.8 mm to 1.2 mm.
- the manufacturing method of this embodiment may further include removing the core 200 from the jelly-roll type electrode assembly 100 .
- the separator 130 contacting the winding core 200 inside the electrode assembly 100 may have a surface roughness value adjusted by the ratio of the first alumina and the second alumina.
- the surface roughness between the winding core 200 and the separator 130 may be adjusted to a predetermined value or less. Therefore, it is possible to minimize the separation membrane 130 being pulled out of the rolled jelly-roll type electrode assembly 100 or the separation membrane 130 being damaged in the process of discharging the winding core 200 .
- the manufacturing method of the jelly-roll type electrode assembly according to the present embodiment described above may be performed by a manufacturing apparatus of a jelly-roll type electrode assembly.
- the manufacturing apparatus includes a transfer unit for transporting the sheet-like assembly, a winding unit for winding the sheet-like assembly, a measuring unit for measuring the surface roughness of the separator 130 or the winding core 200, and the surface of the separator 130 or the winding core 200. It may include a control unit that compares roughness values and calculates a difference value, and a work unit that adjusts the surface roughness of the winding core 200 based on the difference value.
- the winding unit may include the aforementioned winding core 200 .
- the measuring unit may include a non-contact or contact roughness meter for measuring surface roughness.
- the working part may include a sanding device used in a sanding process and a lapping device used in a lapping process.
- the control unit may compare the measured surface roughness values, calculate a difference value, and control the overall operation of the above-described manufacturing apparatus. For example, the control unit may control the measuring unit to measure the surface roughness of the separator 130 or the winding core 200 . For another example, based on the measured value, the control unit may control the operation of the sanding or lapping device to perform the sanding or lapping process.
- Table 3 is a test result of whether problems occurring during the winding process are improved according to the ratio of the first alumina and the second alumina included in the alumina mixture.
- Table 3 it is noted in advance that alumina having a diameter of 500 nm was used as the second alumina in the case of the single-sided SRS, and alumina having a diameter of 300 nm was used as the second alumina in the case of the double-sided SRS.
- the step of adjusting the surface roughness of the winding core according to the manufacturing method of the above-described embodiment was applied, and thus the difference in surface roughness between the winding core and the double-sided SRS separator may be less than or equal to the first value.
- the slip phenomenon may be less likely to occur than the double-sided SRS separator when winding the sheet-like laminate.
- the winding is performed with the core on the side where the coating layer is not formed when winding the sheet-type laminate, fewer problems such as loss of tail or damage to the separator occur than in the case of using a double-sided SRS separator.
- the coating layer of the separator since the coating layer of the separator must be disposed to face the electrode, there is a problem in that the time required for the manufacturing process and the steps of the manufacturing process increase.
- the difference between the surface roughness of the separator 130 and the surface roughness of the winding core may be large. there is.
- a sanding process and a DLC coating process were applied to the winding core for this purpose, but there was a problem that the winding core was not discharged (automatic discharge issue), so it was not suitable for use in this embodiment.
- the automatic discharge issue was solved by applying some processes for adjusting the surface roughness of the winding core, but damage to the separator 130 was confirmed as in the above example.
- the aluminum mixture used in the coating layer of the separator 130 may contain 24wt% or more of the second alumina.
- the ratio of the first alumina and the second alumina may be appropriately adjusted depending on desired surface roughness and physical/electrochemical properties.
- the ratio of the second alumina increases, the surface roughness improves, so that the slip phenomenon, tail loss phenomenon or separator damage phenomenon that occurs during winding core discharge can be improved, but as the ratio of the first alumina having a small particle diameter increases, the air permeability and fixation of the coating layer As it is known that the force can be improved, it may be preferable that the ratio of the second aluminum is included within an appropriate value. For example, it may be appropriate that the second alumina is included within 40 wt% of the alumina mixture. It may be appropriate that the second alumina is included within 24wt% to 40wt% of the alumina mixture.
- an appropriate value of surface roughness may vary depending on the difference in roughness from the winding core, the width of the separator 130, or the size of the jelly-roll type electrode assembly 100.
- the size of the jelly-roll electrode assembly 100 increases, the contact area between the winding core and the separator 130 increases, and the contact area between the rolled separator 130 and the electrodes 110 and 120 also increases, so tail loss phenomenon Alternatively, damage to the separation membrane 130 may occur more frequently.
- the surface roughness value of the separator 130 is designed to be somewhat large, and the jelly-roll type electrode assembly 100 or the core 100a When the length of ) is formed small, it may be desirable to design the surface roughness value of the separator 130 to be somewhat small.
- the length of the core 100a is about 10 to 12 cm, and the radius of the jelly-roll type electrode assembly 100 is 4 to 5 cm. Therefore, when the size of the jelly-roll type electrode assembly 100 is designed to be smaller than this, the preferred ratio of the second alumina may be 24wt% or less.
- the second alumina when the second alumina is included in the alumina mixture at a level of 16wt% or 24wt%, the slip phenomenon does not appear during winding, and the tail loss phenomenon or damage to the separator 130 may not occur during winding core discharge. Therefore, it may be preferable that the second alumina is included in the alumina mixture in an amount of 16wt% or more. It may be appropriate that the second alumina is included within 16wt% to 24wt% of the alumina mixture. It may be appropriate that the second alumina is included within 16wt% to 40wt% of the alumina mixture.
- the surface roughness (Ra) of the double-sided SRS separator may be 500 nm to 1 ⁇ m, preferably 550 nm to 930 nm.
- Ra (nm) a parameter of the surface roughness
- the jelly-roll type electrode assembly 100 may be included in a battery cell.
- the jelly-roll type electrode assembly 100 may be manufactured as a battery cell by inserting the cylindrical or prismatic metal container, filling the electrolyte, and sealing the metal container.
- the battery cell including the jelly-roll type electrode assembly 100 may be a cylindrical battery or a prismatic battery, but the shape of the battery cell including the jelly-roll type electrode assembly 100 is not limited to the above example.
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Abstract
Description
기호 | ▽ ▽ ▽ ▽ | ▽ ▽ ▽ | ▽ ▽ | ▽ | |||||||||||||||
샌딩 | SB | O | O | O | O | O | O | ||||||||||||
래핑 | LP | O | O | O | O |
표면 가공 구분치 | ||||
다듬질 기호 | 호칭명 | Rmax | Rz | Ra |
▽ ▽ ▽ ▽ | 정밀 다듬질 | 0.8s | 0.8z | 0.2a |
▽ ▽ ▽ | 上 다듬질 | 6.3s | 6.3z | 1.6a |
▽ ▽ | 下 다듬질 | 25s | 25z | 6.3a |
▽ | 거친 다듬질 | 100s | 25z | |
~ | 특별한 규정 없음 |
항목 | 단위 | 단면 SRS |
양면 SRS | |||
두께 | μm | 12.9 | 12.6 | 13 | 12.7 | |
basis weight/total weight | g/m2 | 8.29 | 7.9 | 8.3 | 8.21 | |
제1 알루미나 | wt% | 100 | 100 | 84 | 76 | |
제2 알루미나 | - | - | 16 | 24 | ||
Roughness (Ra) |
Top (원단) | Nm | 180 | 201 | 550 | 930 |
Back (SRS) | 610 | |||||
Coefficient of friction (static/kinetic) |
Sanding | μk | (PE) 0.44/0.33 | 0.76/0.72 | 0.67/0.67 | 0.67/0.67 |
Lapping | (SRS) 0.23/0.21 | 0.31/0.28 | 0.27/0.23 | 0.27/0.23 | ||
Winding Test 결과 | ||||||
슬립 현상 | 이슈 없음 | 이슈 없음 | 이슈 없음 | 이슈 없음 | ||
자동 배출 **권심 사양(gap=0.12mm, R=0.6mm) 래핑 공정 또는 샌딩 공정 적용 |
이슈 없음 | 이슈 없음 (Sanding+ 코팅RT5000기준) |
이슈 없음 | 이슈 없음 | ||
분리막 손상 |
Claims (19)
- 전극 및 분리막을 포함하는 시트형 적층체가 권취된 젤리-롤형 전극 조립체에 있어서,상기 분리막은 양면 코팅층을 포함하고,상기 코팅층은 제1 알루미나 및 제2 알루미나의 혼합물을 포함하며,상기 분리막의 표면 거칠기(Ra)는 500nm 내지 1μm 이고, 상기 제1 알루미나의 입자 직경은 상기 제2 알루미나의 입자 직경보다 작은 젤리-롤형 전극 조립체.
- 제1항에서,상기 혼합물 100 중량부에 대하여, 상기 제2 알루미나는 16 내지 40 중량부 로 포함되는 젤리-롤형 전극 조립체.
- 제2항에서,상기 혼합물 100 중량부에 대하여, 상기 제1 알루미나는 60 내지 84 중량부 로 포함되는 젤리-롤형 전극 조립체.
- 제1항에서,상기 제1 알루미나의 입자 직경은 20 내지 50nm 인 젤리-롤형 전극 조립체.
- 제1항에서,상기 제2 알루미나의 입자 직경은 300 내지 500nm 인 젤리-롤형 전극 조립체.
- 제1항에서,상기 전극 조립체는 분리막, 양극, 분리막, 음극의 순서로 적층된 양면 SRS 적층체인 젤리롤형 전극 조립체.
- 제1항에서,상기 젤리롤형 전극 조립체의 코어의 길이는 약 10 cm 내지 12 cm 이고, 반지름은 약 4 cm 내지 5 cm 인 젤리롤형 전극 조립체.
- 양면 코팅층을 포함하는 분리막을 제공하는 단계,상기 분리막 및 권심의 표면 거칠기의 차이 값을 산출하는 단계,상기 분리막과 상기 권심의 표면 거칠기 값의 차이가 제1 값 미만이면, 제1 공정을 이용하여 상기 권심의 표면 거칠기를 조절하고,상기 분리막과 상기 권심의 표면 거칠기 값의 차이가 상기 제1 값 이상이면, 제2 공정을 이용하여 상기 권심의 표면 거칠기를 조절하는 단계, 및상기 표면 거칠기가 조절된 상기 권심을 이용하여, 전극 및 상기 분리막을 포함하는 시트형 적층체를 권취하는 단계를 포함하고,상기 코팅층은 제1 알루미나 및 제2 알루미나의 혼합물을 포함하며,상기 분리막의 표면 거칠기(Ra)는 500nm 내지 1μm 이고, 상기 제1 알루미나의 입자 직경은 상기 제2 알루미나의 입자 직경보다 작은 젤리-롤형 전극 조립체의 제조 방법.
- 제8항에서,상기 혼합물 100 중량부에 대하여, 상기 제2 알루미나는 16 내지 40 중량부 로 포함되는 젤리-롤형 전극 조립체.
- 제9항에서,상기 혼합물 100 중량부에 대하여, 상기 제1 알루미나는 60 내지 84 중량부 로 포함되는 젤리-롤형 전극 조립체.
- 제8항에서,상기 제1 값(Rmax)은 0.05s 내지 0.15s 사이인 젤리-롤형 전극 조립체의 제조 방법.
- 제8항에서,상기 제1 공정은 샌딩 공정인 젤리-롤형 전극 조립체의 제조 방법.
- 제8항에서,상기 제2 공정은 래핑 공정인 젤리-롤형 전극 조립체의 제조 방법.
- 제8항에서,상기 시트형 적층체는 로드(rod)형태의 권심에 의해 권취되고,상기 권심은 회전축을 중심으로 분리된 제1 부분 및 제2 부분을 포함하며,상기 시트형 적층체의 일단은 상기 제1 부분 및 상기 제2 부분 사이의 슬릿에 삽입됨으로써 고정되고,상기 슬릿의 크기는 0.8mm 보다 큰 젤리-롤형 전극 조립체의 제조 방법.
- 제8항에서,상기 시트형 적층체는 로드(rod)형태의 권심에 의해 권취되고,상기 권심의 표면 거칠기는 제2 값 이하이며,상기 제2 값(Rmax)은 0.15 s 내지 0.25s 인 젤리-롤형 전극 조립체의 제조 방법.
- 제8항에서,상기 권심의 표면 거칠기를 조절하는 단계에서 상기 제2 공정이 이용된 경우, 상기 분리막 및 상기 권심의 표면 거칠기의 차이 값을 산출하는 단계가 다시 수행되는 젤리-롤형 전극 조립체의 제조 방법.
- 제16항에서,다시 수행된 상기 분리막 및 상기 권심의 표면 거칠기의 차이 값을 산출하는 단계에서 산출된 표면 거칠기의 차이 값이 제1 값 이상이면, 제2 공정을 이용하여 상기 권심의 표면 거칠기를 조절하는 단계가 수행되는 젤리-롤형 전극 조립체의 제조 방법.
- 제16항에서,다시 수행된 상기 분리막 및 상기 권심의 표면 거칠기의 차이 값을 산출하는 단계에서 산출된 표면 거칠기의 차이 값이 제1 값 미만이면, 제1 공정을 이용하여 상기 권심의 표면 거칠기를 조절하는 단계가 수행되고,상기 표면 거칠기가 조절된 상기 권심을 이용하여, 전극 및 상기 분리막을 포함하는 시트형 적층체를 권취하는 단계가 수행되는 젤리-롤형 전극 조립체의 제조 방법.
- 제1항에 따른 젤리-롤형 전극 조립체를 포함하는 전지셀.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US18/567,641 US20240266585A1 (en) | 2021-07-20 | 2022-07-20 | Jelly-Roll Type Electrode Assembly and Method of Manufacturing the Same |
CN202280033495.0A CN117280507A (zh) | 2021-07-20 | 2022-07-20 | 卷绕型电极组件以及制造该卷绕型电极组件的方法 |
EP22846210.7A EP4310967A4 (en) | 2021-07-20 | 2022-07-20 | ROLLED TYPE ELECTRODE ASSEMBLY AND MANUFACTURING METHOD THEREOF |
JP2023562776A JP2024515074A (ja) | 2021-07-20 | 2022-07-20 | ゼリーロール型電極組立体およびその製造方法 |
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JP2001176540A (ja) * | 1999-12-17 | 2001-06-29 | Toshiba Battery Co Ltd | ニッケル水素二次電池 |
KR100824851B1 (ko) * | 2006-10-27 | 2008-04-23 | 삼성에스디아이 주식회사 | 전극 조립체 및 이를 구비하는 이차 전지 |
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JP2019021805A (ja) * | 2017-07-19 | 2019-02-07 | Jsr株式会社 | 電極体及び蓄電デバイス |
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KR101147604B1 (ko) * | 2007-10-12 | 2012-05-23 | 주식회사 엘지화학 | 젤리-롤형 전극조립체의 변형을 억제하기 위한 제조방법 |
WO2011013300A1 (ja) * | 2009-07-31 | 2011-02-03 | パナソニック株式会社 | 非水電解質二次電池及びその製造方法 |
KR101515357B1 (ko) * | 2012-02-29 | 2015-04-28 | 제일모직주식회사 | 유기 및 무기 혼합물 코팅층을 포함하는 분리막 및 이를 이용한 전지 |
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JP2001176540A (ja) * | 1999-12-17 | 2001-06-29 | Toshiba Battery Co Ltd | ニッケル水素二次電池 |
KR100824851B1 (ko) * | 2006-10-27 | 2008-04-23 | 삼성에스디아이 주식회사 | 전극 조립체 및 이를 구비하는 이차 전지 |
KR20090100207A (ko) * | 2008-03-18 | 2009-09-23 | 시케이디 가부시키가이샤 | 권취 장치, 권회 소자 및 권회 소자의 제조 방법 |
KR101310541B1 (ko) * | 2008-12-24 | 2013-09-23 | 미쓰비시 가가꾸 가부시키가이샤 | 전지용 세퍼레이터 및 비수계 리튬 전지 |
JP2019021805A (ja) * | 2017-07-19 | 2019-02-07 | Jsr株式会社 | 電極体及び蓄電デバイス |
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EP4310967A1 (en) | 2024-01-24 |
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