Method for monitoring the total amount of brighteners in an acidic copper/copper alloy plating bath and controlled process for plating
US-2019078229-A1 · Mar 14, 2019 · US
US10547081B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10547081-B2 |
| Application number | US-201715662785-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 28, 2017 |
| Priority date | Aug 23, 2016 |
| Publication date | Jan 28, 2020 |
| Grant date | Jan 28, 2020 |
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An electrolytic copper foil capable of improving a capacity retention rate of a secondary battery, an electrode including the same, a secondary battery including the same, and a method of manufacturing the same. The electrolytic copper foil, which includes a first surface and a second surface opposite the first surface, includes a copper layer including a matte surface facing the first surface and a shiny surface facing the second surface, and a first protective layer on the matte surface of the copper layer, wherein the first surface has a peak density (PD) of 3 to 110, a texture coefficient [TC(220)] of a (220) plane of 1.32 or less, and a surface roughness (Rz) of 0.5 to 2.7 μm.
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What is claimed is: 1. A method of manufacturing a secondary battery electrolytic copper foil, the method comprising: forming a copper layer by applying electricity between a positive electrode plate and a rotating negative electrode drum which are disposed in an electrolytic solution containing 70 to 90 g/L of copper ions and 50 to 150 g/L of sulfuric acid to be spaced apart from each other; and forming a protective layer on the copper layer, wherein the forming of the copper layer includes: performing a heat treatment on a copper wire; pickling the heat-treated copper wire; preparing the electrolytic solution by introducing the pickled copper wire into sulfuric acid; performing electroplating by applying electricity between the positive electrode plate and the rotating negative electrode drum at a current density of 40 to 80 A/dm 2 ; and performing continuous filtration at a flow rate of 31 to 45 m 3 /hr to remove solid impurities from the electrolytic solution while the electroplating is performed, wherein, while the electroplating is performed, total carbon (TC) in the electrolytic solution is maintained at a range of 0.04 to 0.24 g/L, a concentration of silver (Ag) therein is maintained at a range of 0.03 to 0.19 g/L, and a concentration of iron (Fe) therein is maintained at a range of 0.05 to 0.51 g/L. 2. The method of claim 1 , further comprising: monitoring the concentration of iron (Fe) in the electrolytic solution while the electroplating is performed; and replacing all or some of the electrolytic solution when the concentration of iron (Fe) is more than 0.54 g/L. 3. The method of claim 1 , wherein the copper wire is heat-treated at a temperature of 600 to 900° C. for 30 to 60 minutes. 4. The method of claim 1 , wherein the electrolytic solution further includes chloride ion capable of precipitating silver (Ag) in the form of AgCl in order to prevent the concentration of silver (Ag) from exceeding 0.2 g/L by silver (Ag) being introduced into the electrolytic solution while the electroplating is performed. 5. The method of claim 1 , wherein the forming of the copper layer further includes introducing hydrogen peroxide and air into the electrolytic solution while the electroplating is performed. 6. The method of claim 1 , wherein the electrolytic solution further includes an organic additive selected from a group consisting of hydroxyethyl cellulose (HEC), organic sulfides, organic nitrides, and thiourea-based compounds. 7. The method of claim 1 , wherein the electrolytic solution further includes 1 to 10 ppm of ethylene thiourea. 8. The method of claim 1 , wherein the forming of the copper layer includes polishing a surface of the rotating negative electrode drum with an abrasive brush having #800 to #1500 of a particle-size (Grit). 9. The method of claim 1 , wherein: the forming of the protective layer includes immersing the copper layer in an antirust solution containing 0.5 to 1.5 g/L of Cr; and a concentration of copper (Cu) in the antirust solution is maintained at 0.1 g/L or less. 10. A secondary battery electrolytic copper foil, which is manufactured by the method of claim 1 , and includes a first surface and a second surface opposite the first surface, the electrolytic copper foil comprising: a copper layer including a matte surface facing the first surface and a shiny surface facing the second surface; and a first protective layer on the matte surface of the copper layer, wherein the first surface has a peak density (PD) of 3 to 110, a texture coefficient [TC(220)] of a (220) plane of 1.32 or less, and a surface roughness (R z )) of 0.5 to 2.7 μm. 11. The electrolytic copper foil of claim 10 , further comprising a second protective layer on the shiny surface of the copper layer, wherein the second surface has a PD of 3 to 110, a texture coefficient [TC(220)] of a (220) plane of 1.32 or less, and a surface roughness (R z )) of 0.5 to 2.7 μm. 12. The electrolytic copper foil of claim 11 , wherein: a difference between the PDs of the first and second surfaces is 95 or less; a difference between the texture coefficients [TC(220)] of the (220) planes of the first and second surfaces is 0.53 or less; and, a difference between the surface roughnesses (R z ) of the first and second surfaces is 0.8 μm or less. 13. The electrolytic copper foil of claim 12 , wherein each of the first and second protective layers includes chromium (Cr). 14. The electrolytic copper foil of claim 10 , wherein the electrolytic copper foil has a yield strength of 21 to 63 kgf/mm 2 and an elongation of 3% or more at room temperature. 15. A secondary battery electrode comprising: an electrolytic copper foil being manufactured by the method of claim 1 , and including a first surface and a second surface opposite the first surface; and a first active material layer on the first surface of the electrolytic copper foil, wherein the electrolytic copper foil includes: a copper layer including a matte surface facing the first surface and a shiny surface facing the second surface; and a first protective layer on the matte surface of the copper layer, and wherein the first surface has a PD of 3 to 110, a texture coefficient [TC(220)] of a (220) plane of 1.32 or less, and a surface roughness (R z ) of 0.5 to 2.7 μm. 16. The secondary battery electrode of claim 15 , wherein: the electrolytic copper foil further includes a second protective layer on the shiny surface of the copper layer; the secondary battery electrode further includes a second active material layer on the second protective layer; and the second surface has a PD of 3 to 110, a texture coefficient [TC(220)] of a (220) plane of 1.32 or less, and a surface roughness (R z ) of 0.5 to 2.7 μm. 17. The secondary battery electrode of claim 16 , wherein: a difference between the PDs of the first and second surfaces is 95 or less; a difference between the texture coefficients [TC(220)] of the (220) planes of the first and second surfaces is 0.53 or less; and a difference between the surface roughnesses (R z ) of the first and second surfaces is 0.8 μm or less. 18. The secondary battery electrode of claim 16 , wherein each of the first and second active material layers comprises at least one active material selected from a group consisting of carbon, a metal such as Si, Ge, Sn, Li, Zn, Mg, Cd, Ce, Ni, or Fe, an alloy containing the metal, an oxide of the metal, and a composite of the metal and carbon. 19. The secondary battery electrode of claim 18 , wherein each of the first and second active material layers comprises Si. 20. A secondary battery comprising: a cathode; an anode opposite to the cathode and including a secondary battery electrode; an electrolyte configured to provide an environment in which lithium ions may move between the cathode and the anode; and a separator configured to electrically insulate the cathode from the anode, wherein the secondary battery electrode is manufactured by the method of claim 1 , and comprises: an electrolytic copper foil including a first surface and a second surface opposite the first surface; and a first active material layer on the first surface of the electrolytic copper foil, wherein the electrolytic copper foil includes: a copper layer including a matte surface facing the first surface and a shiny surface facing the second surface; and a first protective layer on the matte surface of the copper layer, and wherein the first surface has a PD of 3 to 110, a texture coefficient
Separation of the formed objects from the electrodes {with no destruction of said electrodes} · CPC title
by coating on an electrolyte layer · CPC title
Electroforming · CPC title
by electrochemical processing (electroless electrochemical plating C23C18/54) · CPC title
Silicon or alloys based on silicon · CPC title
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