CN110042438B - Method for preparing electrolytic copper foil - Google Patents
Method for preparing electrolytic copper foil Download PDFInfo
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- CN110042438B CN110042438B CN201910335218.5A CN201910335218A CN110042438B CN 110042438 B CN110042438 B CN 110042438B CN 201910335218 A CN201910335218 A CN 201910335218A CN 110042438 B CN110042438 B CN 110042438B
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- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
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Abstract
The invention provides a preparation method of an electrolytic copper foil, which comprises the following steps of S1, preparing a copper sulfate electrolyte: heating and dissolving high-purity copper wires with the purity of 99.95 percent or more in a sulfuric acid solution to generate a copper sulfate electrolyte; s2, manufacturing a raw foil; adding an additive into the copper sulfate electrolyte, and conveying the copper sulfate electrolyte into an electrolytic tank of a foil forming machine for electrolytic foil forming, wherein the copper sulfate electrolyte is used for electrolytic foil forming; the technological parameters of the electrolytic green foil are as follows: the temperature of the electrolyte is controlled to be 50-60 ℃, and the current density of the anode plate in the foil generation process is 38-45A/dm2，Cu2+The concentration is 90-95 g/L, H2SO4The concentration is 100-110 g/L, the gelatin concentration is 100-300ppm, the concentration of ceric sulfate is 0.5-10 ppm, the concentration of MESS is 1-20 ppm, the concentration of SPS is 10-50 ppm, Cl‑The concentration is 10-30 ppm; s3, anti-oxidation treatment: carrying out anti-oxidation treatment on the copper foil obtained by electrolysis; s4, slitting the product: and cutting, cutting and packaging the copper foil subjected to the anti-oxidation treatment.
Description
Technical Field
The invention relates to a preparation method of an electrolytic copper foil.
Background
At present, copper foil is an indispensable important basic material in the electronic industry, and particularly, as the new energy industry is further upgraded, the 6 μm or less electrolytic copper foil has wider market prospect, and the quality requirement on the 6 μm or less electrolytic copper foil is higher and higher. Therefore, development and research of a method for producing a high-hardness electrolytic copper foil of 6 μm or less are urgently required.
Disclosure of Invention
The invention provides a preparation method of an electrolytic copper foil, which can effectively solve the problems.
The invention is realized by the following steps:
a method for preparing an electrolytic copper foil comprises the following steps:
s1, preparing a copper sulfate electrolyte: heating and dissolving high-purity copper wires with the purity of 99.95 percent or more in a sulfuric acid solution to generate a copper sulfate electrolyte;
s2, manufacturing a raw foil; adding an additive into the copper sulfate electrolyte, and conveying the copper sulfate electrolyte into an electrolytic tank of a foil forming machine for electrolytic foil forming, wherein the copper sulfate electrolyte is used for electrolytic foil forming; the technological parameters of the electrolytic green foil are as follows: the temperature of the electrolyte is controlled to be 50-60 ℃, and the current density of the anode plate in the foil generation process is 38-45A/dm2，Cu2+The concentration is 90-95 g/L, H2SO4The concentration is 100-110 g/L, the gelatin concentration is 100-300ppm, the concentration of ceric sulfate is 0.5-10 ppm, the concentration of MESS is 1-20 ppm, the concentration of SPS is 10-50 ppm, Cl-The concentration is 10-30 ppm;
s3, anti-oxidation treatment: carrying out anti-oxidation treatment on the copper foil obtained by electrolysis;
s4, slitting the product: and cutting, cutting and packaging the copper foil subjected to the anti-oxidation treatment.
As a further improvement, Cu2+The concentration is 92-95 g/L, H2SO4The concentration is 105-108 g/L, and the temperature of the electrolyte is controlled at 55-60 ℃.
As a further improvement, the gelatin concentration is 150-250ppm, the ceric sulfate concentration is 2-5 ppm, and the MESS concentration is 10-15 ppm.
As a further improvement, the concentration of SPS is 20-30 ppm, and Cl is-The concentration is 25-30 ppm.
As a further improvement, in step S3, the step of subjecting the copper foil obtained by electrolysis to an oxidation preventing treatment includes:
s31, passivating the copper foil obtained by electrolysis in a CrO3+ T (chromium trioxide + glucose) solution, wherein the passivation parameters are as follows: controlling pH at 3-3.5, temperature at 20-40 deg.C, and passivation current at 1-3A/dm2。
As a further improvement, in step S31, the passivation parameters are: the temperature is controlled at 25-30 ℃, and the passivation current is controlled at 2A/dm2。
The invention has the beneficial effects that: the invention can effectively solve the problems of the following control in the production process by finely controlling the electrolyte indexes: the uniformity deviation is large, and abnormal problems such as pinholes, oxidation color difference of the roll surface of the cathode roll, edge tearing and the like are caused; the strength of the electrolytic copper foil can be remarkably improved, the tensile strength of the electrolytic copper foil is 600-560 MPa at normal temperature, and the tensile strength of the electrolytic copper foil after being heated for 15 minutes at 150 ℃ is 350-400 MPa. In addition, because the production speed of 6 microns or less is high, the time for passing through the passivation tank is shortened, the previously used 6-12 micron preparation method cannot meet the production requirements of 6 micron or less electrolytic copper foil, and the abnormal conditions of oxidation resistance failure and the like can be effectively solved by controlling passivation parameters in the passivation process.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings that are required to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
FIG. 1 is a schematic diagram of a foil generation apparatus according to an embodiment of the present invention.
Fig. 2 is a schematic view of a partial structure of an anode unit in a foil generating device according to an embodiment of the present invention.
FIG. 3 is a schematic diagram of a part of the structure of a cathode roller in a foil generating device according to an embodiment of the present invention.
FIG. 4 is a schematic view of a part of a cleaning unit in a foil generating apparatus according to an embodiment of the present invention.
Fig. 5 is a schematic view of a part of the structure of a conveying unit in a foil generating device according to an embodiment of the present invention.
FIG. 6 is a schematic diagram of a drying and cooling unit in a foil forming apparatus according to an embodiment of the present invention.
FIG. 7 is a flowchart of a method for manufacturing an electrolytic copper foil according to an embodiment of the present invention.
FIG. 8 is a SEM photograph of a bright side of an electrodeposited copper foil with an electrolytic copper foil according to an embodiment of the present invention.
FIG. 9 is a scanning electron micrograph of a matte surface in the electrolytic copper foil according to the example of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention more apparent, the technical solutions of the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings of the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all embodiments of the present invention. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention. Thus, the following detailed description of the embodiments of the present invention, presented in the figures, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention.
In the description of the present invention, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implying any number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless specifically defined otherwise.
Referring to fig. 1, an embodiment of the present invention provides a foil generation apparatus 100, including: the device comprises an anode unit 10, a cathode roller 20, a cleaning unit 30, a conveying unit 40, a drying and cooling unit 50, a winding unit 60 and a passivation tank 80, wherein the cleaning unit 30, the conveying unit 40, the drying and cooling unit 50, the winding unit 60 and the passivation tank are arranged on one side of the cathode roller 20. The anode unit 10 is connected with the positive pole of a direct current power supply, and the cathode roller 20 is connected with the negative pole of the direct current power supply.
Referring to fig. 2, the anode unit 10 includes two arc-shaped anode slots 11 coaxially disposed and a plurality of anode plates 12 disposed on the arc-shaped anode slots 11. The bottom between the two arc anode slots 11 is arranged at intervals, so that a liquid inlet 13 is formed. The anode plates 12 are sequentially spliced on the surface of the arc-shaped anode groove 11 from two sides of the liquid inlet 13 to the upper ends of two sides of the arc-shaped anode groove 11 in the radial direction respectively. The top of the arc anode groove 11 is provided with a liquid drainage channel 112.
The liquid inlet 13 comprises a plurality of shunting guide plates 14 arranged at intervals, and the shunting guide plates 14 are arranged between the two arc-shaped anode slots 11 in the vertical direction, so that the liquid inlet 13 is divided into a plurality of liquid inlet shunting guide channels. Each liquid inlet split flow guide channel is provided with a valve (not shown in the figure) respectively, so that the flow of each liquid inlet split flow guide channel can be controlled. And then the flow of the respective liquid inlet shunting guide channels is controlled, so that the fine control of the whole surface density of the rapidly produced ultrathin copper foil 70 is realized, the transverse uniformity of the copper foil 70 is improved, and the soft wrinkles and the seersucker are reduced. Preferably, the device comprises 10 to 20 flow dividing guide plates 14 arranged at intervals. In this embodiment, the liquid inlet 13 is divided into 16 uniform inlet liquid diversion guide channels by 15 diversion guide plates 14 arranged at intervals. As a further improvement, the drainage channels 112 are embedded in the arc-shaped anode grooves 11. More specifically, the inlet of the drainage channel 112 is arranged at the upper end of the intrados of the arc anode slot 11 and above the topmost anode plate 12; the outlet of the liquid drainage channel 112 is arranged outside the outer arc surface of the arc anode groove 11 and is opened downwards.
As a further improvement, the guiding flow distribution plate 14 is of a rectangular parallelepiped structure and is respectively connected with the arc anode slots 11 on both sides.
As a further improvement, the bottom surface of the anode plate 12 is an arc surface attached to the inner arc surface of the arc anode slot 11, and the adjacent anode plates 12 are attached and connected through side planes.
As a further improvement, a conductive interface (not shown in the figure) is disposed on the lower surface of each anode plate 12, and each anode plate 12 is connected to an independent dc power supply respectively and adjusts the input current by the respective independent dc power supply.
As a further improvement, conductive through holes (not shown) are respectively arranged on the arc-shaped anode slots 11 at positions corresponding to the conductive interfaces.
Referring to fig. 3, the cathode roll 20 includes a roll surface 21 for raw foil and side portions 22 disposed at two sides of the roll surface 21; the surface roughness of the roll surface 21 satisfies: ra <0.2mm, Rz <1.5 mm; the edge 22 is formed by hydrogen peroxide oxidation. By finely grinding the roll surface 21, pinholes in the surface of the ultra-thin copper foil 70 produced rapidly can be effectively eliminated. In addition, the processing of the side portion 22 is also advantageous to solve the problem that the ultra-thin copper foil 70, which is produced at a high speed, is easily broken during the peeling process.
As a further improvement, the width of the side part 22 is preferably 20-30 mm. In one embodiment, the width of the lip 22 is about 25 mm. The cathode roll 20 is a titanium roll.
The cathode roll 20 may be prepared by:
s1, dividing the surface of the cathode roll 20 into a roll surface 21 of green foil and side portions 22 provided on both sides of the roll surface 21;
s2, grinding the roll surface 21 with a grinding wheel so that the roughness of the roll surface 21 satisfies: ra <0.2mm, Rz <1.5 mm;
and S3, oxidizing the edge 22 by using hydrogen peroxide.
As a further improvement, in step S2, the roll surface 21 is ground with grinding wheels of 80#, 120#, 220#, 320#, 400#, 600# and 800# in order to make the roughness of the roll surface 21 satisfy: ra <0.2mm, Rz <1.5 mm.
As a further improvement, in step S3, the step of oxidizing the side 22 with hydrogen peroxide includes:
the edge 22 is wiped and wetted with hydrogen peroxide.
Referring to fig. 4, the cleaning unit 30 includes a collecting plate 31, a flexible water receiving plate 32 disposed on the collecting plate 31, a spray pipe 33, and a plurality of spray heads 34 disposed on the spray pipe 33 side by side; the flow rate of each nozzle 34 is 20-30L/H, and the pressure is 0.25-0.30 MPa. In the process of rapidly manufacturing the ultra-thin copper foil 70, since the speed is too fast and the cleaning time is short, it is necessary to increase the amount of water for cleaning and to ensure that a large amount of cleaning water cannot flow into the electrolyte.
As a further improvement, the flexible water receiving plate 32 is a PVC soft plate, and the thickness of the PVC soft plate is 0.1-0.5 mm. In one embodiment, the thickness of the PVC flexible sheet is 0.3mm, so that the concentration of the solution is ensured not to be diluted under the condition that the foil surface is not scratched, and the problem of cleaning the surface of the rapidly produced ultrathin copper foil 70 is effectively solved.
As a further improvement, the cleaning unit 30 comprises 10-20 spray heads 34 arranged on the spray pipe 33 side by side. Preferably, the cleaning unit 30 comprises 14 to 16 spray heads 34 arranged on the spray pipe 33 side by side. In one embodiment, the cleaning unit 30 includes 15 spray heads 34 arranged side by side on the spray pipe 33, and two adjacent spray heads 34 are arranged in a crossing manner.
As a further improvement, the cleaning unit 30 may further include a wringing glue roller 35 disposed at the top of the spray head 34 and tangent to the cathode roller 20 to squeeze the moisture remaining on the copper foil 70.
The transfer unit 40 includes a peeling roller 41, a first transfer roller 42, a second transfer roller 43, and a third transfer roller 44, each having a diameter of 200mm or more and 300mm or less. The peeling roller 41 is disposed at the top of the cleaning unit 30, the passivation tank 80 is disposed at one side of the peeling roller 41, the second conductive roller 43 is disposed in the passivation tank 80, and the first conductive roller 42 and the third conductive roller 44 are symmetrically disposed at the top of the passivation tank 80; the first transfer roller 42 employs a double pair of bearings.
In one embodiment, each guide roller 42/43/44 has a diameter of about 250 mm. The rapidly produced ultrathin copper foil 70 is conducted by a large-roll-diameter conducting roller for more than 200mm, so that the stress of the foil surface can be dispersed, and the problem that the rapidly produced ultrathin copper foil 70 is easy to wrinkle in the conducting process is effectively solved. Meanwhile, the design of double pairs of bearings is adopted on a single transmission roller, so that the resistance of the transmission roller is reduced as much as possible, and the transmission can be driven by adopting smaller tension, thereby further effectively solving the problem that the rapidly produced ultrathin copper foil 70 is easy to wrinkle in the transmission process.
As a further improvement, the conveying unit 40 may employ closed-loop control to make the tension fluctuation of the copper foil 70 less than 0.3KG, so that bubble sand generated by the tension fluctuation may be effectively solved.
Referring to fig. 5, as a further improvement, the first transmission roller 42 includes a transmission roller main body 420, a first bearing 421, a rotation shaft 422, a second bearing 423 and a support seat 424; the first bearing 421 is sleeved between the conductive roller body 420 and the rotating shaft 422; both ends of the first bearing 421 are disposed on the supporting seat 424 through the second bearing 423.
The winding unit 60 comprises a winding roller 62 with the diameter of 250-350 mm, and the winding tension of the winding roller is controlled to be 12-14 kg. As a further modification, the winding unit 60 further includes a lower pressure roller 63 disposed below the winding roller 62. According to the invention, the winding roller with the diameter of 250-350 mm is used for winding the rapidly produced ultrathin copper foil 70, the winding tension is controlled between 12-14, and simultaneously, the lower pressing roller 63 is added during winding based on the fine control of the surface density of the ultrathin copper foil 70, so that the rapidly produced ultrathin copper foil 70 is more flat and compact in winding without soft lines, and the end face consistency during winding is ensured.
As a further improvement, the winding unit 60 further includes a fourth transmission roller 62 disposed on a side of the third transmission roller 44 far away from the first transmission roller 42, and the fourth transmission roller 62, the third transmission roller 44 and the first transmission roller 42 are disposed side by side. The wind-up roll 62 is disposed at the lower end of the fourth transfer roll 62 far away from the first transfer roll 42.
Referring to fig. 6, the drying and cooling unit 50 is disposed between the passivation tank 80 and the winding unit 60; the drying and cooling unit 50 includes a drying unit 51 disposed adjacent to the transfer unit 40, and a cooling unit 52 disposed adjacent to the winding unit 60; the drying unit 51 comprises an upper hot air knife 512 and a lower hot air knife 514 which are symmetrically arranged, and a hot air pipeline 516 connected with the upper hot air knife 512 and the lower hot air knife 514; cooling unit 52 includes the symmetry setting go up cold wind sword 522 and cold wind sword 524 down, and connect in go up cold wind sword 522 and cold wind pipeline 526 of cold wind sword 524 down. The ultra-thin copper foil 70 foil surface quickly produced by the invention is dried by adopting a double-sided air knife, the front row is uniformly and quickly blown out by using high-temperature hot air, and the rear row is uniformly and quickly blown out by using cold air, so that the fastest drying and cooling are ensured.
As a further improvement, the flow rate of the drying unit 51 is 400m3H, and the temperature is 90-100 ℃. The flow rate of the cooling unit 52 was 210m3H, and the temperature is 20-27 ℃.
Referring to fig. 7, the present invention further provides a method for preparing an electrolytic copper foil, including the steps of:
s4, preparing a copper sulfate electrolyte: heating and dissolving high-purity copper wires with the purity of 99.95 percent or more in a sulfuric acid solution to generate a copper sulfate electrolyte;
s5, manufacturing a raw foil; adding an additive into the copper sulfate electrolyte, and conveying the copper sulfate electrolyte into an electrolytic tank of a foil forming machine for electrolytic foil forming, wherein the copper sulfate electrolyte is used for electrolytic foil forming; the technological parameters of the electrolytic green foil are as follows: the temperature of the electrolyte is controlled to be 50-60 ℃, and the current density of the anode plate 12 in the foil generation process is 38-45A/dm2，Cu2+The concentration is 90-95 g/L, H2SO4The concentration is 100-110 g/L, the gelatin concentration is 100-300ppm, the concentration of ceric sulfate is 0.5-10 ppm, the concentration of MESS is 1-20 ppm, the concentration of SPS is 10-50 ppm, Cl-The concentration is 10-30 ppm;
s6, anti-oxidation treatment: carrying out anti-oxidation treatment on the copper foil obtained by electrolysis;
s7, slitting the product: and cutting, cutting and packaging the copper foil subjected to the anti-oxidation treatment.
In step S5, preferably, Cu2+The concentration is 92-95 g/L, H2SO4The concentration is 105-108 g/L, and the temperature of the electrolyte is controlled at 55-60 ℃. The gelatin concentration is 150-250ppm, the ceric sulfate concentration is 2-5 ppm, and the MESS concentration is 10-15 ppm. The concentration of the SPS is 20-30 ppm, and Cl is-The concentration is 25-30 ppm. The combination of the aqueous solution A containing ceric sulfate and MESS can be adsorbed near the surface of an electrode, so that the cathode polarization is effectively improved, the crystal grains are refined, and the crystal grain size of a coating is changed, thereby improving the hardness of the coating; containing SPS and Cl-The combination of the aqueous solution B can remarkably improve the brightness of the plating layer.
In step S6, the step of subjecting the copper foil obtained by electrolysis to oxidation prevention treatment includes:
s61, passivating the copper foil obtained by electrolysis in a CrO3+ T (chromium trioxide + glucose) solution, wherein the passivation parameters are as follows: controlling pH at 3-3.5, temperature at 20-40 deg.C, and passivation current at 1-3A/dm2. Because the production speed of the 4-6 micron ultrathin copper foil is high and the time for passing through the passivation tank 80 is shortened, the previously used 8-12 micron preparation method cannot meet the production requirements of the 4-6 micron electrolytic copper foil, so that the electrolytic copper foil is ineffective in oxidation resistance. The invention uses the preparation process of CrO3+ T, controls the PH to be 3-3.5, the temperature to be 20-40 ℃ and the passivation current to be 1-3A, thereby effectively solving the abnormal situations such as oxidation resistance failure and the like.
In step S61, it is preferable that the passivation parameter is: the temperature is controlled at 25-30 ℃, and the passivation current is controlled at 2A/dm2。
Referring to fig. 8-9, the invention also provides an electrolytic copper foil obtained by the above method, wherein the thickness of the electrolytic copper foil is 4-6 microns, the tensile strength at normal temperature is 600-560 MPa, the tensile strength after heating at 150 ℃ for 15 minutes is 350-400 MPa, and the elongation at normal temperature and after heating at 150 ℃ for 15 minutes is 3.5-10%; and the warpage of the high-strength electrolytic copper foil is less than or equal to 5 mm. The high-strength electrolytic copper foil is warped by placing a copper foil sample with the length and the width larger than 15cm on pearl cotton with the bright surface facing upwards; then, placing the disc sampler on a copper foil sample; pressing down a handle and clockwise rotating for 180 degrees to cut into a circular sample; and (3) turning the round sample to enable the rough surface to face upwards by using a steel ruler, and finally measuring the warping of the edge part 22 of the round sample by using the steel ruler.
As a further improvement, the glossiness of the rough surface of the high-strength electrolytic copper foil is 130-250 Gu.
As a further improvement, the gloss of the bright surface of the high-strength electrolytic copper foil is 60-100 Gu.
As a further improvement, the high-strength electrolytic copper foil has a uniform areal density of 30 to 60 g/m.
The invention also provides a lithium ion secondary battery current collector and a lithium ion secondary battery using the high-strength electrolytic copper foil.
In addition, the invention also provides an electromagnetic shielding material prepared by using the high-strength electrolytic copper foil.
Example (b): heating and dissolving a high-purity copper wire with the purity of 99.95% in a sulfuric acid solution to generate a copper sulfate electrolyte; adding an additive into the copper sulfate electrolyte, and conveying the copper sulfate electrolyte into an electrolytic tank of a foil forming machine for electrolytic foil forming, wherein the copper sulfate electrolyte is used for electrolytic foil forming; the technological parameters of the electrolytic green foil are as follows: the temperature of the electrolyte is controlled at 58 ℃, and Cu2+The concentration is 94g/L, H2SO4106g/L of gelatin, 150ppm of gelatin, 4ppm of ceric sulfate, 12ppm of MESS, 25ppm of SPS, and Cl-The concentration is 28 ppm; the copper foils with the diameters of 4 microns, 4.5 microns, 5 microns and 6 microns are respectively obtained by controlling the current density of the anode plate in the foil generation process. The test data for various copper foils were as follows:
the above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (3)
1. The preparation method of the electrolytic copper foil is characterized by comprising the following steps:
s1, preparing a copper sulfate electrolyte: heating and dissolving high-purity copper wires with the purity of 99.95 percent or more in a sulfuric acid solution to generate a copper sulfate electrolyte;
s2, manufacturing a raw foil; adding an additive into the copper sulfate electrolyte, and conveying the copper sulfate electrolyte into an electrolytic tank of a foil forming machine for electrolytic foil forming, wherein the copper sulfate electrolyte is used for electrolytic foil forming; the technological parameters of the electrolytic green foil are as follows: the temperature of the electrolyte is controlled to be 50-60 ℃, the current density of the anode plate in the foil forming process is 38-45A/dm < 2 >, the concentration of Cu2+ is 90-95 g/L, the concentration of H2SO4 is 100-110 g/L, the concentration of gelatin is 100-300ppm, the concentration of ceric sulfate is 0.5-10 ppm, the concentration of MESS is 1-20 ppm, the concentration of SPS is 20-30 ppm, and the concentration of Cl-is 25-30 ppm; winding the copper foil prepared by electrolysis by using a winding roller with the thickness of 250-350 mm, wherein the winding tension is controlled to be 12-14 kg;
s3, anti-oxidation treatment: carrying out anti-oxidation treatment on the copper foil obtained by electrolysis;
s4, slitting the product: cutting, cutting and packaging the copper foil subjected to the anti-oxidation treatment;
in step S3, the step of subjecting the copper foil obtained by electrolysis to oxidation prevention treatment includes:
s31, passivating the copper foil obtained by electrolysis in a CrO3+ T solution, wherein the passivation parameters are as follows: controlling the pH value to be 3-3.5, the temperature to be 25-30 ℃ and the passivation current to be 2A/dm 2;
in step S4, the cutting and slitting into the warp of the high-strength electrolytic copper foil is performed by placing a copper foil sample sheet with a length and a width of more than 15cm on pearl wool with a bright surface facing upward; then, placing the disc sampler on a copper foil sample; pressing down a handle and clockwise rotating for 180 degrees to cut into a circular sample; and (3) turning the round sample to enable the rough surface to face upwards by using a steel ruler, and finally measuring the warping of the edge of the round sample by using the steel ruler to obtain the round sample.
2. The method for producing an electrolytic copper foil according to claim 1, wherein the concentration of Cu2+ is 92 to 95g/L, the concentration of H2SO4 is 105 to 108g/L, and the temperature of the electrolyte is controlled to 55 to 60 ℃.
3. The method of manufacturing electrolytic copper foil according to claim 1, wherein the concentration of gelatin is 150-250ppm, the concentration of ceric sulfate is 2-5 ppm, and the concentration of MESS is 10-15 ppm.
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| CN114182308B (en) * | 2021-12-01 | 2023-11-10 | 江西省科学院能源研究所 | Additive for preparing electrolytic copper foil and preparation method of electrolytic copper foil |
| CN117364181A (en) * | 2022-06-30 | 2024-01-09 | 比亚迪股份有限公司 | Copper foil, preparation method and lithium ion battery |
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