IP Library Granted Patent US 11,380,898
Granted Patent B2
US 11,380,898 · App. 16/343,500 · Granted Jul 5, 2022

Electrolytic copper foil for secondary battery and method for producing the same

Inventors: Sun Hyoung Lee (Iksan, KR); Tae Jin Jo (Iksan, KR); Seul-Ki Park (Iksan, KR); Ki Deok Song (Iksan, KR)
Assignee: ILJIN MATERIALS CO., LTD.
H01M4/661C25D1/04C25D17/12
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Quick Facts
Patent No.
US 11,380,898
App. No.
16/343,500
Granted
Jul 5, 2022
Kind
B2
Abstract

The present invention relates to an electrolytic copper foil for a secondary battery and a method of producing the same, and more particularly, to an electrolytic copper foil for a secondary battery, which has little change in a physical property of a copper foil before and after vacuum drying in a process of producing an electrolytic copper foil, thereby exhibiting excellent cycle life in a battery test at a high-density negative electrode, and preventing cracking. The electrolytic copper foil for a secondary battery is produced from a plating solution containing Total Organic Carbon (TOC), zinc, and iron by using a drum, in which a ratio of the TOC to the zinc and the iron contained in the electrolytic copper foil follows Formula 1 below: TOC/(zinc+iron)=1.3 to 1.5   Formula 1

Claims (23)

1. An electrolytic copper foil for a secondary battery, comprising:

a first layer that contains total organic carbon (TOC) and metallic additives that contain zinc, and iron,

wherein the first layer is produced from a plating solution containing TOC, zinc, and iron by using a drum, and wherein a concentration of the TOC contained in the plating solution is in a range of 450 ppm-1080 ppm,

wherein a ratio of the TOC to the zinc and the iron contained in the first layer follows Formula 1 below:

TOC/(zinc+iron)=1.3 to 1.5.  Formula 1

2. The electrolytic copper foil of claim 1 , wherein a negative electrode active material is applied to the first layer and wherein, upon performing a vacuum drying process to the electrolytic copper foil having the negative electrode active material, a ratio of tensile strength and elongation percentages of the electrolytic copper foil having the negative electrode active material before and after the vacuum drying process follows Formula 2 below:

((tensile strength after vacuum drying/tensile strength before vacuum drying)/(elongation percentage after vacuum drying/elongation percentage before vacuum drying)×tensile strength after vacuum drying)=28 to 50 kgf/mm 2 , and  Formula 2

wherein the vacuum drying process is performed at a temperature range of 110° C. to 150° C. for 6 hours to 10 hours.

3. The electrolytic copper foil of claim 1 , wherein, upon performing a vacuum drying process to the electrolytic copper foil, a ratio of tensile strength after the vacuum drying process to tensile strength before the vacuum drying process follows Formula 3 below:

Tensile strength after vacuum drying/tensile strength before vacuum drying=0.8 to 1.01, and  Formula 3

wherein the vacuum drying process is performed at a temperature range of 110° C. to 150° C. for 6 hours to 10 hours.

4. The electrolytic copper foil of claim 1 , wherein, upon performing a vacuum drying process to the electrolytic copper foil, a ratio of an elongation percentage after the vacuum drying process to an elongation percentage before the vacuum drying process follows Formula 4 below:

Elongation percentage after vacuum drying/elongation percentage before vacuum drying=0.9 to 1.4, and  Formula 4

wherein the vacuum drying process is performed at a temperature range of 110° C. to 150° C. for 6 hours to 10 hours.

5. The electrolytic copper foil of claim 1 , wherein tensile strength of the electrolytic copper foil at room temperature is 39.5 kgf/mm 2 to 48.4 kgf/mm 2 .

6. The electrolytic copper foil of claim 1 , wherein a thickness of the electrolytic copper foil is 4 μm to 12 μm.

7. The electrolytic copper foil of claim 1 , wherein an elongation percentage of the electrolytic copper foil is 2% to 18%.

8. The electrolytic copper foil of claim 1 , wherein a negative electrode active material is applied to the first layer and wherein, upon performing a vacuum drying process to the electrolytic copper foil having the negative electrode active material, a ratio of tensile strength and elongation percentages of the electrolytic copper foil having the negative electrode active material before and after the vacuum drying process follows Formula 2 below:

((tensile strength after vacuum drying/tensile strength before vacuum drying)/(elongation percentage after vacuum drying/elongation percentage before vacuum drying)×tensile strength after vacuum drying)=28 to 50 kgf/mm 2 .  Formula 2

9. The electrolytic copper foil of claim 1 , wherein, upon performing a vacuum drying process to the electrolytic copper foil, a ratio of tensile strength after the vacuum drying process to tensile strength before the vacuum drying process follows Formula 3 below:

Tensile strength after vacuum drying/tensile strength before vacuum drying=0.8 to 1.01.  Formula 3

10. The electrolytic copper foil of claim 1 , wherein, upon performing a vacuum drying process to the electrolytic copper foil, a ratio of an elongation percentage after the vacuum drying process to an elongation percentage before the vacuum drying process follows Formula 4 below:

Elongation percentage after vacuum drying/elongation percentage before vacuum drying=0.9 to 1.4.  Formula 4

Assignments (2)
CHANGE OF NAME Recorded Aug 31, 2023
From: ILJIN COPPER FOIL CO., LTD.
To: LOTTE ENERGY MATERIALS CORPORATION
Reel/Frame 064786/0928 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 19, 2019
From: LEE, SUN HYOUNG; JO, TAE JIN; PARK, SEUL-KI; SONG, KI DEOK
To: ILJIN MATERIALS CO., LTD.
Reel/Frame 048942/0094 →
Priority Claims (1)
KR 10-2016-0150350 · Nov 11, 2016 · national
Continuity (1)
Related Publication 20190334177A1 · Oct 31, 2019