Method for manufacturing copper foil with rough surface in plating tank and its product
11008665 · 2021-05-18
Assignee
Inventors
Cpc classification
Y10T428/12431
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
Y10T428/12993
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
International classification
B21C37/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method for manufacturing a copper foil with a rough surface in a plating tank includes causing an electrolyte solution to flow between an anode and a cathode with a current density of 5 ASF-40 ASF. The copper foil with a rough surface including dense nodules of single copper crystals is deposited on the cathode. The electrolyte solution includes chloride ions (20 ppm-80 ppm), polyethylene glycol (PEG) with a molecular weight of 400-8000 (100 ppm-700 ppm), sulfuric acid (20 g/L-200 g/L), copper sulfate pentahydrate (70 g/L-320 g/L) and a sulfur compound (1 ppm-60 ppm).
Claims
1. A copper foil, being an electro-deposited copper foil with a rough surface; wherein the rough surface comprises dense nodules of single copper crystals and has an arithmetic mean roughness (Ra) of 0.20 μm-1.5 μm and a ten-point mean roughness (Rz) of 0.5 μm-8.0 μm, wherein the nodules of single copper crystals are integrally formed with the copper foil and in the form of specific shapes.
2. The copper foil of claim 1, wherein the copper foil excluding the nodules of single copper crystals has a thickness of 2.5 μm-5.0 μm.
3. The copper foil of claim 1, wherein the nodules of single copper crystals are in the form of stepped cones, eggs or grains.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
(3)
(4)
(5)
(6)
(7)
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
(8)
(9) Operating conditions and components of the electrolyte solution 30 are as follows:
(10) current density: 5 ASF-40 ASF;
(11) temperature: 20° C.-25° C.;
(12) chloride ions: 20 ppm-80 ppm;
(13) polyethylene glycol (PEG, the preferred wetting agent, having a molecular weight of 400-8000): 100 ppm-700 ppm;
(14) sulfuric acid: 20 g/L-200 g/L;
(15) copper sulfate pentahydrate: 70 g/L-320 g/L; and a sulfur compound having the formula (1): 1 ppm-60 ppm,
R.sub.1—S—C.sub.nH.sub.2n—R.sub.2 (1),
(16) wherein R.sub.1 is —H, —C.sub.7H.sub.4NS, —CH.sub.4N.sub.2, —S—C.sub.nH.sub.2n—R.sub.2 or —C.sub.nH.sub.2n—R.sub.2, R.sub.2 is —SO.sub.3.sup.−, —PO.sub.4.sup.− or —COO.sup.−.Math., and n is an integer of 2-10.
(17) According to the formula (1), the preferred sulfur compound is selected from the group consisting of 3-mercaptopropanesulfonate (MPS), bis-(3-sulfopropyl)-disulfide (SPS), 3-(2-benzthiazolylthio)-1-propanesulfonate (ZPS), 3-(N,N-dimethylthiocarbamoyl)-thiopropanesulfonate (DPS), (o-ethyldithiocarbonato)-s-(3-sulfopropyl)-ester (OPX), 3-[(amino-iminomethyl)thio]-1-propanesulfonate (UPS) and 3,3-thiobis(1-propanesulfonate) (TBPS).
(18) Through the process with the above plating tank, conditions and the electrolyte solution, a raw copper foil having a thickness of 3 μm-5 μm is formed on the cathode. As shown in
Example 1
(19) The electrolyte solution includes chloride ions (30 ppm-60 ppm), polyethylene glycol (PEG) having a molecular weight of 400-5000 (100 ppm-700 ppm), sulfuric acid (20 g/L-200 g/L), copper sulfate pentahydrate (70 g/L-250 g/L) and a sulfur compound (1 ppm-15 ppm).
(20)
(21)
(22)
Example 2
(23) The electrolyte solution includes chloride ions (50 ppm-80 ppm), polyethylene glycol (PEG) having a molecular weight of 4000-8000 (100 ppm-700 ppm), sulfuric acid (20 g/L-200 g/L), copper sulfate pentahydrate (70 g/L-250 g/L) and a sulfur compound (15 ppm-60 ppm).
(24)
(25)
Example 3
(26) The electrolyte solution includes chloride ions (60 ppm-80 ppm), polyethylene glycol (PEG) having a molecular weight of 4000-8000 (100 ppm-700 ppm), sulfuric acid (20 g/L-200 g/L), copper sulfate pentahydrate (70 g/L-250 g/L) and a sulfur compound (40 ppm-60 ppm).
(27)
(28)
Example 4
(29) The electrolyte solution includes chloride ions (40 ppm-80 ppm), polyethylene glycol (PEG) having a molecular weight of 1000-2500 (50 ppm-300 ppm), sulfuric acid (100 g/L-200 g/L), copper sulfate pentahydrate (120 g/L-220 g/L) and a sulfur compound (40 ppm-60 ppm).
(30)
(31)
Example 5
(32) The electrolyte solution includes chloride ions (40 ppm-80 ppm), polyethylene glycol (PEG) having a molecular weight of 1000-3000 (100 ppm-300 ppm), sulfuric acid (200 g/L-300 g/L), copper sulfate pentahydrate (100 g/L-200 g/L) and a sulfur compound (5 ppm-30 ppm).
(33)
(34)
(35) Summarily, the electro-deposition process is improved as the rough surface of the copper foil can be achieved simultaneously in one plating tank. The rough surface includes uniform and dense nodules of single copper crystals having specific outlooks. Compared with the traditional methods, this invention is more efficient and therefore saves a lot of cost. The single copper crystals with the rough surface have lower electric resistance than the roughed matte sides formed by the traditional methods and can be controlled in shapes and sizes by changing the components of the electrolyte solution.