Coating apparatus, coating method, method for manufacturing a positive electrode, and method for manufacturing a solid battery
The coating apparatus and method address the issue of drag during intermittent slurry discharge by using die heads and gas ejection units to improve shape accuracy, particularly for positive electrode composite and insulating layers in solid batteries.
Patent Information
- Authority / Receiving Office
- JP · JP
- Patent Type
- Patents
- Current Assignee / Owner
- HONDA MOTOR CO LTD
- Filing Date
- 2024-03-29
- Publication Date
- 2026-04-23
AI Technical Summary
Existing coating apparatuses experience drag at the end of the slurry when it is discharged intermittently from the die head, leading to reduced shape accuracy of the coating.
A coating apparatus and method that includes a conveying unit, first and second die heads for intermittent slurry discharge perpendicular to the conveying direction, and first and second gas ejection units to eject gas parallel to the conveying direction, with specific nozzle and body configurations to suppress drag and improve shape accuracy.
The solution effectively suppresses drag at the end of the slurry, enhancing the shape accuracy of the coating, particularly in the formation of positive electrode composite and insulating layers, which is crucial for solid batteries.
Smart Images

Figure 0007850760000002 
Figure 0007850760000003 
Figure 0007850760000004
Abstract
Description
Technical Field
[0001] The present invention relates to a coating apparatus, a coating method, a method for manufacturing a positive electrode, and a method for manufacturing a solid battery.
Background Art
[0002] In recent years, in order to enable many people to access affordable, reliable, sustainable, and advanced energy, research and development on batteries that contribute to energy efficiency have been carried out.
[0003] A battery includes a positive electrode having a positive electrode current collector and a positive electrode mixture layer, a negative electrode having a negative electrode current collector and a negative electrode mixture layer, and an electrolyte. When manufacturing the battery, a coating apparatus is used.
[0004] Patent Document 1 describes a coating apparatus that applies a slurry to the surface of a continuously moving sheet-like member. Here, the coating apparatus includes a die head having a slit-shaped discharge port facing a backup roll that supports the sheet-like member. Further, the coating apparatus is disposed on the side of the sheet-like member at a position immediately after the discharge port, and is provided with a first gas nozzle directed to supply pressurized gas in a direction along the width direction to the edge in the width direction of the slurry layer applied to the sheet-like member. Furthermore, the coating apparatus is provided with a second gas nozzle disposed downstream of the first gas nozzle and on the backup roll toward the end in the width direction of the slurry layer, and directed to supply pressurized gas in a direction perpendicular to the surface of the slurry layer.
Prior Art Documents
Patent Documents
[0005]
Patent Document 1
Summary of the Invention
Problems to be Solved by the Invention
[0006] However, in the coating apparatus described in Patent Document 1, when slurry is discharged intermittently from the die head, drag occurs at the end of the discharged slurry.
[0007] The present invention aims to provide a coating apparatus and a coating method that can suppress drag at the end of the discharged slurry, even when the slurry is discharged intermittently from the die head. [Means for solving the problem]
[0008] (1) A conveying unit for continuously conveying a sheet-like material to be coated; a first die head for intermittently discharging a first slurry toward a first surface region of the continuously conveyed material to be coated to intermittently form a first coated region; and a first gas ejection unit for ejecting a first gas toward the end of the intermittently discharged first slurry, wherein the first die head discharges the first slurry in a direction substantially perpendicular to the conveying direction of the material to be coated in the first surface region and has a slit-shaped first discharge port extending in the width direction of the conveying unit; and the first gas ejection unit is located in the direction of conveying the material to be coated in the first surface region A coating apparatus comprising a slit-shaped first nozzle extending in the width direction of the conveying section, which ejects the first gas in a substantially parallel direction, and a first main body and a second main body extending in the width direction of the conveying section, wherein the first nozzle is formed between the first main body and the second main body, and the first gas ejection section is arranged such that the first nozzle is near the first discharge port, and the first main body and the second main body are on the side of the first die head and the conveying section, respectively, and the first main body extends further toward the first die head than the second main body.
[0009] (2) The coating apparatus according to (1), wherein the first gas ejection section further comprises a plurality of first supply ports to which the first gas is supplied, and a first gas confluence section connected to the plurality of first supply ports and the first ejection port, to which the first gas supplied from the plurality of first supply ports merges, and the plurality of first supply ports are arranged in the width direction of the conveying section.
[0010] (3) The coating apparatus according to (2), wherein the first supply port and the first gas confluence have dimensions larger than the first nozzle in the thickness direction, and the first gas confluence has an inclined surface that is inclined toward the first nozzle.
[0011] (4) The coating apparatus according to (2) or (3), wherein the first main body portion has a groove-shaped portion extending in the width direction of the conveying portion, the second main body portion is a plate-shaped member, and the first gas confluence portion is formed between the first main body portion and the second main body portion.
[0012] (5) The coating apparatus according to any one of (1) to (4), further comprising a second die head that intermittently discharges a second slurry toward a second surface region of a continuously conveyed material to be coated to intermittently form a second coating portion, wherein the second surface region is located downstream of the first surface region and the second coating portion is formed in a region where the first coating portion has not been formed, and the second die head discharges the second slurry in a direction substantially perpendicular to the conveying direction of the material to be coated in the second surface region and has a slit-shaped second discharge port extending in the width direction of the conveying portion.
[0013] (6) The coating apparatus according to (5), further comprising a second gas ejection section that ejects a second gas toward the terminal end of the intermittently discharged second slurry, wherein the second gas ejection section ejects the second gas in a direction substantially parallel to the conveying direction of the material to be coated in the second surface region, and has a slit-shaped second nozzle extending in the width direction of the conveying section, and a third body section and a fourth body section extending in the width direction of the conveying section, the second nozzle being formed between the third body section and the fourth body section, the second gas ejection section being arranged such that the second nozzle is near the second discharge port, and the third body section and the fourth body section are on the side of the second die head and the conveying section, respectively, and the third body section extends further toward the second die head than the fourth body section.
[0014] (7) A coating method using a coating apparatus described in any one of (1) to (4), comprising the step of intermittently discharging the first slurry from the first die head toward a first surface region of the sheet-like material to be coated while continuously conveying the sheet-like material to be coated, thereby intermittently forming a first coated portion.
[0015] A coating method using a coating apparatus described in (8)(5) or (6), comprising the steps of: intermittently discharging the first slurry from the first die head toward a first surface region of the sheet-like material to be coated while continuously conveying the sheet-like material to be coated, thereby intermittently forming a first coated portion; and intermittently discharging the second slurry from the second die head toward a second surface region of the continuously conveyed material to be coated, thereby intermittently forming a second coated portion.
[0016] A method for manufacturing a positive electrode by the coating method described in (9)(8), wherein the material to be coated is a positive electrode current collector, the first slurry is a slurry for a positive electrode composite layer, and the second slurry is a slurry for an insulating layer.
[0017] A method for manufacturing a solid battery, comprising the step of obtaining a positive electrode by the method for manufacturing a positive electrode described in (10)(9). [Effects of the Invention]
[0018] According to the present invention, it is possible to provide a coating apparatus and a coating method that can suppress drag at the end of the discharged slurry even when the slurry is discharged intermittently from the die head. [Brief explanation of the drawing]
[0019] [Figure 1] This is a perspective view showing a coating apparatus according to one embodiment of the present invention. [Figure 2] This is a cross-sectional view showing the coating apparatus in Figure 1. [Figure 3] This is a top view illustrating the first coating section. [Figure 4]It is a top view showing dragging at the end of the first slurry. [Figure 5] It is an enlarged perspective view of the first air nozzle of FIG. 2. [Figure 6] It is an enlarged cross-sectional view of the first air nozzle of FIG. 2. [Figure 7] It is a cross-sectional view showing the coating device of FIG. 1. [Figure 8] It is a top view explaining the second coating part. [Figure 9] It is an enlarged cross-sectional view of the second air nozzle of FIG. 2. [Embodiment for Carrying Out the Invention]
[0020] Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0021] [Coating Device] As shown in FIGS. 1 and 2, the coating device 10 includes a conveying roller 11 as a conveying unit for continuously conveying a sheet-shaped coating material M, and a first die head 12 that intermittently discharges the first slurry L1 toward the first surface region S1 of the continuously conveyed coating material M to intermittently form a first coating part C1 (see FIG. 3). Further, the coating device 10 further includes a first air nozzle 13 as a first gas ejection unit that ejects the first gas A1 toward the end of the first slurry L1 discharged intermittently. For this reason, dragging at the end of the first slurry L1 discharged from the first die head 12 is suppressed, and as a result, the shape accuracy of the first coating part C1 is improved. Here, the first die head 12 discharges the first slurry L1 in a direction substantially perpendicular to the conveying direction D1 of the coating material M in the first surface region S1. Further, the first air nozzle 13 ejects the first gas A1 in a direction substantially parallel to the conveying direction D1 of the coating material M in the first surface region S1.
[0022] In order to inject the first gas A1 toward the terminal end of the intermittently discharged first slurry L1, the timing of injecting the first gas A1 should be adjusted based on the coating speed of the first slurry L1 (convection speed of the material to be coated M), the flow velocity of the first gas A1, and the timing of stopping the discharge of the first slurry L1.
[0023] In this case, the coating speed of the first slurry L1 (conveying speed of the material to be coated M) is not particularly limited, but for example, it is 10 m / min or more and 60 m / min or less. Also, the ejection pressure of the first gas A1 is not particularly limited, but for example, it is 10 kPa or more and 700 kPa or less. Furthermore, the viscosity of the first slurry L1 at 25°C is not particularly limited, but for example, it is 1000 mPa·s or more and 3000 mPa·s or less.
[0024] Furthermore, if the first gas A1 is not injected towards the end of the intermittently discharged first slurry L1, drag will occur at the end of the first slurry L1 discharged from the first die head 12 (see Figure 4).
[0025] The first die head 12 discharges the first slurry L1 and has a slit-shaped first discharge port 12a that extends in the width direction W of the conveying roller 11 (material to be coated M). The first air nozzle 13 ejects the first gas A1 and has a slit-shaped first nozzle 13a that extends in the width direction W of the conveying roller 11 (see Figure 5). This further improves the shape accuracy of the first coated section C1. In this case, the first nozzle 13a is located near the first discharge port 12a. The width of the first nozzle 13a is not particularly limited, but for example, it is between 500 mm and 700 mm.
[0026] As shown in Figure 6, the first air nozzle 13 has a first body portion 61 and a second body portion 62 that extend in the width direction W of the conveying roller 11, and the first outlet 13a is formed between the first body portion 61 and the second body portion 62. At this time, the first body portion 61 and the second body portion 62 are arranged so as to be on the side of the first die head 12 and the conveying roller 11 (material to be coated M), respectively, and the first body portion 61 extends further toward the first die head 12 than the second body portion 62 (see Figure 2). Therefore, the first air nozzle 13 can be brought closer to the first discharge port 12a of the first die head 12 to efficiently eject the first gas A1. Furthermore, because the first body portion 61 extends further toward the first die head 12 than the second body portion 62, the first gas A1 is guided toward the end of the intermittently discharged first slurry L1, and the first air nozzle 13 does not interfere with the conveying roller 11.
[0027] The first air nozzle 13 further includes a plurality of first supply ports 63 into which the first gas A1 is supplied from a supply source (e.g., a tank), and a first gas confluence section 64 connected to the plurality of first supply ports 63 and the first outlet 13a, into which the first gas A1 supplied from the plurality of first supply ports 63 converges. In this case, the plurality of first supply ports 63 are formed in the width direction W (depth direction in the figure) of the conveyor roller 11.
[0028] The first supply port 63 and the first gas confluence 64 have dimensions larger than the first nozzle 13a in the thickness direction, and the first gas confluence 64 has an inclined surface I1 that slopes toward the first nozzle 13a. That is, the first main body 61 has a groove-shaped portion G1 that extends in the width direction W of the conveying roller 11, the second main body 62 is a plate-shaped member, and the first gas confluence 64 is formed between the first main body 61 and the second main body 62. In this case, the inclination angle of the inclined surface I1 is not particularly limited, but for example, it is 10° or more and 80° or less.
[0029] The first die head 12 is not particularly limited, and any known die head can be used as long as it is capable of intermittently discharging the first slurry L1 to intermittently form the first coated portion C1.
[0030] As shown in Figure 7, the coating apparatus 10 further includes a second die head 14 that intermittently discharges a second slurry L2 toward a second surface region S2 of the continuously conveyed material M to be coated, thereby intermittently forming a second coated section C2 (see Figure 8). In this case, the second surface region S2 is located downstream of the first surface region S1, and the second coated section C2 is formed in an area where the first coated section C1 has not been formed. As a result, the shape accuracy of the second coated section C2 is also high, along with the shape accuracy of the first coated section C1. Here, the second die head 14 discharges the second slurry L2 in a direction substantially perpendicular to the conveying direction D2 of the material M to be coated in the second surface region S2.
[0031] Furthermore, the coating apparatus 10 is further equipped with a second air nozzle 15, which serves as a second gas ejection unit that ejects a second gas A2 toward the terminal end of the intermittently discharged second slurry L2. As a result, drag at the terminal end of the second slurry L2 discharged from the second die head 14 is suppressed, and consequently, the shape accuracy of the second coated section C2 is improved. Here, the second air nozzle 15 ejects the second gas A2 in a direction substantially parallel to the transport direction D2 of the material to be coated M in the second surface region S2.
[0032] In order to inject the second gas A2 toward the terminal end of the intermittently discharged second slurry L2, the timing of injecting the second gas A2 should be adjusted based on the coating speed of the second slurry L2 (convection speed of the material to be coated M), the flow velocity of the second gas A2, and the timing of stopping the discharge of the second slurry L2.
[0033] In this case, the coating speed of the second slurry L2 (conveying speed of the material to be coated M) is not particularly limited, but for example, it is 10 m / min or more and 60 m / min or less. Also, the ejection pressure of the second gas A2 is not particularly limited, but for example, it is 10 kPa or more and 700 kPa or less. Furthermore, the viscosity of the second slurry L2 at 25°C is not particularly limited, but for example, it is 1000 mPa·s or more and 3000 mPa·s or less.
[0034] The second die head 14, like the first die head 12, discharges the second slurry L2 and has a slit-shaped second discharge port 14a that extends in the width direction W of the conveying roller 11. The second air nozzle 15, like the first air nozzle 13, ejects the second gas A2 and has a slit-shaped second nozzle 15a that extends in the width direction W of the material M to be coated. As a result, the shape accuracy of the second coated section C2 is further improved. In this case, the second nozzle 15a is located near the second discharge port 14a.
[0035] As shown in Figure 9, the second air nozzle 15 has a third body portion 71 and a fourth body portion 72 that extend in the width direction W of the conveying roller 11, and the first nozzle outlet 15a is formed between the third body portion 71 and the fourth body portion 72. At this time, the second body portion 71 and the third body portion 72 are positioned so as to be on the side of the second die head 14 and the conveying roller 11 (material to be coated M), respectively, and the third body portion 71 extends further toward the second die head 14 than the fourth body portion 72 (see Figure 7). Therefore, the second air nozzle 15 can be brought closer to the first discharge port 14a of the first die head 14 to efficiently eject the second gas A2. Furthermore, because the third body portion 71 extends further toward the second die head 14 than the fourth body portion 72, the second gas A2 is guided toward the end of the intermittently discharged second slurry L2, and the second air nozzle 15 does not interfere with the conveying roller 11.
[0036] The second air nozzle 15 further includes a plurality of second supply ports 73 into which the second gas A2 is supplied from a supply source (e.g., a tank), and a second gas confluence section 74 connected to the plurality of second supply ports 73 and the second outlet 15a, into which the second gas A2 supplied from the plurality of second supply ports 73 converges. In this case, the plurality of first supply ports 73 are formed in the width direction W (depth direction in the figure) of the conveyor roller 11.
[0037] The second supply port 73 and the second gas confluence section 74 have dimensions larger than the second nozzle 15a in the thickness direction, and the second gas confluence section 74 has an inclined surface I2 that slopes toward the second nozzle 15a. That is, the third main body 71 has a groove-shaped portion G2 that extends in the width direction W of the conveying roller 11, the fourth main body 72 is a plate-shaped member, and the second gas confluence section 74 is formed between the third main body 71 and the fourth main body 72. In this case, the inclination angle of the inclined surface I2 is not particularly limited, but for example, it is 10° or more and 80° or less.
[0038] The second die head 14 is not particularly limited, and any known die head can be used as long as it is capable of intermittently discharging the second slurry L2 to intermittently form the second coating portion C2.
[0039] Furthermore, the second air nozzle 15 may be omitted if necessary, and the second die head 14 may be omitted as well.
[0040] [Coating method] The coating method of this embodiment includes a step of intermittently discharging a first slurry L1 from a first die head 12 toward a first surface region S1 of a sheet-like material to be coated M while continuously conveying the material, thereby intermittently forming a first coated portion C1, and can be carried out using a coating apparatus 10. At this time, a first gas A1 is ejected toward the terminal end of the intermittently discharged first slurry L1. As a result, drag at the terminal end of the first slurry L1 discharged from the first die head 12 is suppressed, and as a result, the shape accuracy of the first coated portion C1 is improved. Furthermore, the first slurry L1 is discharged in a direction substantially perpendicular to the conveying direction D1 of the material to be coated M in the first surface region S1, and the first gas A1 is ejected in a direction substantially parallel to the conveying direction D1 of the material to be coated M in the first surface region S1.
[0041] The coating method of this embodiment may further include a step of intermittently discharging a second slurry L2 from a second die head 14 toward a second surface region S2 of the continuously conveyed material M to be coated, thereby intermittently forming a second coated portion C2. In this case, the second surface region S2 is located downstream of the first surface region S1, and the second coated portion C2 is formed in an area where the first coated portion C1 has not been formed. As a result, the shape accuracy of the second coated portion C2 is also high, along with the shape accuracy of the first coated portion C1. Here, the second slurry L2 is discharged in a direction substantially perpendicular to the conveying direction D2 of the material M to be coated in the second surface region S2.
[0042] In this embodiment, the coating method may involve ejecting a second gas A2 toward the terminal end of the intermittently discharged second slurry L2. At this time, the second gas A2 is ejected in a direction substantially parallel to the transport direction D2 of the material to be coated M in the second surface region S2. As a result, drag at the terminal end of the second slurry L2 discharged from the second die head 14 is suppressed, and as a result, the shape accuracy of the second coated section C2 is improved. Here, the second gas A2 is ejected in a direction substantially parallel to the transport direction D2 of the material to be coated M in the second surface region S2.
[0043] The coating method of this embodiment may further include a step of heating and drying the material to be coated M on which the first coated portion C1 (and the second coated portion C2) is formed.
[0044] Furthermore, the coating method of this embodiment can be applied, for example, to the manufacture of the positive electrode, negative electrode, and solid electrolyte layer that constitute a battery.
[0045] [Manufacturing method for positive electrode] The positive electrode manufacturing method of this embodiment is a method of manufacturing a positive electrode by the coating method of this embodiment. Here, the material to be coated M is a positive electrode current collector, the first slurry is a slurry for the positive electrode composite layer, and the second slurry is a slurry for the insulating layer. As a result, a positive electrode with high shape accuracy of the positive electrode composite layer and insulating layer can be obtained.
[0046] The positive electrode current collector is not particularly limited, but an example is aluminum foil.
[0047] The slurry for the positive electrode composite layer includes, for example, a positive electrode active material. The positive electrode active material is not particularly limited, but an example is lithium iron phosphate.
[0048] The slurry for the insulating layer contains an insulating material. The insulating material is not particularly limited, but alumina is an example.
[0049] The method for manufacturing the positive electrode of this embodiment may further include a step of continuously forming a second insulating layer on both sides in the width direction W of the positive electrode composite layer. In this case, the second insulating layer may also be formed when forming the positive electrode composite layer.
[0050] [Manufacturing method for solid-state batteries] The manufacturing method for the solid-state battery of this embodiment includes a step of obtaining a positive electrode using the positive electrode manufacturing method of this embodiment. Therefore, short circuits in the solid-state battery are suppressed.
[0051] The method for manufacturing a solid-state battery according to this embodiment may further include a step of forming a solid electrolyte layer on a positive electrode composite layer to form a positive electrode-solid electrolyte layer laminate.
[0052] Solid-state batteries are not particularly limited, but examples include all-solid-state lithium metal batteries. All-solid-state lithium metal batteries will be described below.
[0053] An all-solid-state lithium metal battery comprises a negative electrode having a negative electrode current collector and a lithium metal layer, a positive electrode having a positive electrode current collector and a positive electrode composite layer, and a solid electrolyte layer.
[0054] The negative electrode current collector is not particularly limited, but an example is copper foil.
[0055] The positive electrode composite layer contains a positive electrode active material and may further contain a solid electrolyte, a conductive additive, a binder, etc. The positive electrode active material is not particularly limited as long as it is capable of intercalating and releasing lithium ions, but examples include lithium nickel cobalt manganese composite oxide. The solid electrolyte is not particularly limited as long as it has lithium ion conductivity, but examples include oxide-based electrolytes and sulfide-based electrolytes. The conductive additive is not particularly limited as long as it has electronic conductivity, but examples include carbon black. The binder is not particularly limited as long as it can improve binding properties, but examples include styrene butadiene rubber.
[0056] The positive electrode current collector is not particularly limited, but an example is aluminum foil.
[0057] The solid electrolyte layer contains a solid electrolyte and may further contain a binder or the like. The solid electrolyte is not particularly limited as long as it has lithium ion conductivity, but examples include inorganic solid electrolytes such as oxide-based electrolytes and sulfide-based electrolytes. The binder is not particularly limited as long as it can improve the binding properties, but examples include styrene-butadiene rubber.
[0058] Furthermore, an intermediate layer having the function of uniformly depositing lithium metal may be formed between the negative electrode and the solid electrolyte layer. This stabilizes the interface between the intermediate layer and the solid electrolyte layer. In this case, the all-solid-state lithium metal battery may be an anode-free battery in which the lithium metal layer is not formed at the time of the first charge. In an anode-free battery, the lithium metal layer is formed after the first charge and discharge.
[0059] The intermediate layer contains a metal that can alloy with lithium and amorphous carbon, and may further contain a binder. The metal that can alloy with lithium and amorphous carbon are preferably nanoparticles. Examples of metals that can alloy with lithium include tin (Sn), silicon (Si), zinc (Zn), magnesium (Mg), gold (Au), platinum (Pt), palladium (Pd), silver (Ag), aluminum (Al), bismuth (Bi), and antimony (Sb). Examples of amorphous carbon include carbon blacks such as acetylene black, furnace black, and Ketjen black, as well as coke and activated carbon. The amorphous carbon may be easily graphitizable carbon (soft carbon), difficult-to-graphitize carbon (hard carbon), CNT (carbon nanotube), fullerene, or graphene. The binder is not particularly limited as long as it can improve binding properties, but an example is polyvinylidene fluoride (PVDF).
[0060] Although embodiments of the present invention have been described above, the present invention is not limited to the above embodiments, and the above embodiments may be modified as appropriate within the scope of the spirit of the present invention. [Examples]
[0061] The following describes embodiments of the present invention, but the present invention is not limited to these embodiments.
[0062] [Example 1] A positive electrode composite layer was intermittently formed on the positive electrode current collector using a coating apparatus 10. Specifically, while continuously conveying aluminum foil as the material to be coated M, a slurry for the positive electrode composite layer, called the first slurry L1, was intermittently discharged from the first die head 12 toward the first surface region S1 of the continuously conveyed material to be coated M, thereby intermittently forming a positive electrode composite layer, called the first coated section C1. At this time, the first gas A1 was ejected from the first air nozzle 13 toward the terminal end of the intermittently discharged first slurry L1. Here, the slurry for the positive electrode composite layer was a slurry containing lithium iron phosphate as the positive electrode active material, with a viscosity of 2000 mPa·s or more and 2500 mPa·s or less at 25°C, and the first air nozzle 13 was an air nozzle having a first nozzle 13a with a width of 1 mm. Furthermore, the coating speed of the first slurry L1 (the conveying speed of the material to be coated M) was set to 10 m / min, and the ejection pressure of the first gas A1 was set to 500 kPa.
[0063] [Comparative Example 1] Except for not ejecting the first gas A1 from the first air nozzle 13 toward the terminal end of the intermittently discharged first slurry L1, the positive electrode composite layer was intermittently formed on the positive electrode current collector in the same manner as in Example 1.
[0064] [Comparative Example 2] Except for using a blowback-type air knife instead of the first air nozzle 13, the positive electrode composite layer was intermittently formed on the positive electrode current collector, similar to Example 1.
[0065] [Dragging] The drag at the end of the discharged first slurry L1 was measured.
[0066] Table 1 shows the results of the drag evaluation.
[0067] [Table 1]
[0068] Table 1 shows that in Example 1, the drag is reduced. In contrast, in Comparative Example 1, the first gas A1 was not ejected from the first air nozzle 13 toward the terminal end of the intermittently discharged first slurry L1, resulting in greater drag at the terminal end of the discharged first slurry L1. In Comparative Example 2, the first gas A1 was ejected, resulting in less drag than in Comparative Example 1. However, since the air knife does not have a first body portion 61 and a second body portion 62, it cannot be brought close to the first discharge port 12a of the first die head 12, and therefore the first gas A1 cannot be efficiently ejected. As a result, the drag is greater than in Example 1. [Explanation of Symbols]
[0069] 10 Coating equipment 11 Conveyor rollers 12. First Die Head 12a 1st outlet 13. First air nozzle 13a 1st spout 14. Second Die Head 14a 2nd outlet 15. Second air nozzle 15a 2nd spout 61 First main body 62 Second Main Body 63 1st supply port 64 First Gas Confluence 71 Third Main Body 72 Fourth main body 73 2nd supply port 74 Second Gas Confluence A1 First Gas A2 Second Gas C1 First Coating Section C2 Second Coating Section D1, D2 Conveying direction G Groove I Inclined surface L1 First Slurry L2 Second Slurry M Covered material S1 1st surface area S2 2nd surface area W (width direction)
Claims
1. A conveying unit that continuously transports sheet-like materials to be coated, A first die head intermittently discharges a first slurry toward the first surface region of the material to be coated, which is continuously conveyed, to intermittently form a first coated area. The system includes a first gas ejection unit that ejects a first gas toward the terminal end of the intermittently discharged first slurry in such a manner that dragging at the terminal end of the first slurry is suppressed. The first die head discharges the first slurry in a direction perpendicular to the conveying direction of the material to be coated in the first surface region, and has a slit-shaped first discharge port extending in the width direction of the conveying section. The first gas ejection unit ejects the first gas in a direction parallel to the conveying direction of the material to be coated in the first surface region, and has a slit-shaped first nozzle extending in the width direction of the conveying unit, and a first main body and a second main body extending in the width direction of the conveying unit. The first nozzle is formed between the first main body and the second main body, The first gas ejection unit is arranged such that the first ejection port is near the first discharge port, and the first main body and the second main body are located on the side of the first die head and the conveying unit, respectively. A coating apparatus wherein the first main body extends further toward the first die head than the second main body.
2. The first gas ejection unit further comprises a plurality of first supply ports to which the first gas is supplied, and a first gas confluence unit connected to the plurality of first supply ports and the first ejection port, to which the first gas supplied from the plurality of first supply ports merges. The coating apparatus according to claim 1, wherein the plurality of first supply ports are arranged in the width direction of the conveying section.
3. The first supply port and the first gas confluence have dimensions larger than the first nozzle in the thickness direction. The coating apparatus according to claim 2, wherein the first gas confluence section has an inclined surface that slopes toward the first nozzle.
4. The first main body has a groove-shaped portion that extends in the width direction of the conveying section, The second main body is a plate-shaped member, The coating apparatus according to claim 2 or 3, wherein the first gas confluence is formed between the first main body and the second main body.
5. The conveying section is a conveying roller, The coating apparatus according to any one of claims 1 to 3, wherein the first surface region has a curved shape corresponding to the curved shape of the surface of the conveying roller.
6. The system further comprises a second die head that intermittently discharges a second slurry toward the second surface region of the continuously conveyed material to be coated, thereby intermittently forming a second coated area. The second surface region is located downstream of the first surface region. The second coating portion is formed in the region where the first coating portion is not formed. The coating apparatus according to claim 1, wherein the second die head discharges the second slurry in a direction perpendicular to the conveying direction of the material to be coated in the second surface region and has a slit-shaped second discharge port extending in the width direction of the conveying section.
7. The system further includes a second gas ejection section that ejects a second gas toward the terminal end of the intermittently discharged second slurry, in order to suppress drag at the terminal end of the second slurry. The second gas ejection unit ejects the second gas in a direction parallel to the conveying direction of the material to be coated in the second surface region, and has a slit-shaped second nozzle extending in the width direction of the conveying unit, and a third body part and a fourth body part extending in the width direction of the conveying unit. The second nozzle is formed between the third main body and the fourth main body, The second gas ejection unit is arranged such that the second ejection port is near the second discharge port, and the third and fourth main body units are positioned on the sides of the second die head and the conveying unit, respectively. The coating apparatus according to claim 6, wherein the third main body extends further toward the second die head than the fourth main body.
8. A method of coating using a coating apparatus according to any one of claims 1 to 3, A coating method comprising the step of intermittently discharging the first slurry from the first die head toward a first surface region of the sheet-like material to be coated while continuously conveying the sheet-like material to be coated, thereby intermittently forming a first coated area.
9. A method of coating using the coating apparatus described in claim 6 or 7, A step of continuously conveying the sheet-like material to be coated, and intermittently discharging the first slurry from the first die head toward the first surface region of the continuously conveyed material to be coated to intermittently form the first coated portion, A coating method comprising the step of intermittently discharging a second slurry from a second die head toward a second surface region of a material to be coated that is continuously conveyed, thereby intermittently forming a second coated area.
10. A method for manufacturing a positive electrode by the coating method described in claim 9, The material to be coated is a positive electrode current collector, The first slurry is a slurry for the positive electrode composite layer, The second slurry is a slurry for an insulating layer, and the method for manufacturing a positive electrode.
11. A method for manufacturing a solid battery, comprising the step of obtaining a positive electrode by the method for manufacturing a positive electrode described in claim 10.
Citation Information
Patent Citations
Coating device
JP2001006664A
Slurry coating device and slurry coating method
JP2017170312A
Coating method and coating device
JP2019130491A