Patent DE685165C successfully refreshed from Google Patents.
Patent US5863410A successfully refreshed from Google Patents.
US5863410A
Expired / Lapsed
US
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Process for the manufacture of high quality very low profile copper foil and copper foil produced thereby
Assignee: Circuit Foil USA Inc
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Filing: 1997-06-23
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Granted: 1999-01-26
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Expires: 2017-06-23
Abstract
Abstract An electrolytic process for producing copper foil having a low profile surface exhibiting a high peel strength when bonded to a polymeric substrate, which process comprises: (a) preparing an electrolyte comprising a copper sulfate-sulfuric acid solution, containing as addition agents, a low molecular weight water-soluble cellulose ether, a low molecular weight water-soluble polyalkylene glycol ether, a low molecular weight water-soluble polyethylene imine and a water-soluble sulfonated organic sulfur compound; (b) passing an electric current through the electrolyte from a primary anode to a cathode spaced from the primary anode in a first electrodeposition zone under first mass transfer conditions including a first current density to electrodeposit on the cathode a base copper foil having a fine-grained microstructure and a matte surface having micropeaks with a height not greater than about 150 microinches; (c) passing the base foil and electrolyte from the first electrodeposition zone to a second electrodeposition zone; and (d) passing an electric current through the electrolyte from a secondary anode to the cathode spaced from the secondary electrode in the second electrodeposition zone under second mass transfer conditions including a second current density greater than the first current density and which provide a mass transfer poorer than that in the first electrodeposition zone, while introducing into the second electrodeposition zone a supplemental stream of the electrolyte, to electrodeposit on the matte surface micronodules of copper, so as to produce a copper foil having a total matte height not greater than about 200 microinches. The produced foil can be passed directly to a station for applying a barrier layer, a station for applying a stain-proofing layer and a station for applying an adhesion promoter to the foil.
Inventors
- 👤 Charles B. Yates
- 👤 Chintsai T. Cheng
- 👤 Adam M. Wolski
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 11:45
CPC Classifications
H; H05; H05K; H05K3/00; H05K3/38; H05K3/382; H05K3/384; C; C25; C25D; C25D1/00; C25D1/04; C25D3/00; C25D3/02; C25D3/38; C25D5/00; C25D5/48; C25D7/00; C25D7/06; C25D7/0614; C25D7/0635; H05K2201/00; H05K2201/03; H05K2201/0332; H05K2201/0335; H05K2201/0355; H05K2203/00; H05K2203/03; H05K2203/0307; H05K2203/07; H05K2203/0703; H05K2203/0723; H05K3/22; H05K3/24; H05K3/241
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
245 words
An electrolytic process for producing copper foil having a low profile surface exhibiting a high peel strength when bonded to a polymeric substrate, which process comprises: (a) preparing an electrolyte comprising a copper sulfate-sulfuric acid solution, said solution having added thereto minor amounts of a low molecular weight water-soluble cellulose ether, a low molecular weight water-soluble polyalkylene glycol ether, a low molecular weight water-soluble polyethyleneimine and a water-soluble sulfonated organic sulfur compound; (b) passing a direct electric current through the electrolyte from a primary anode to a cathode spaced from the primary anode in a first electrodeposition zone under first mass transfer conditions including a first current density to electrodeposit on the cathode a base copper foil having a fine-grained microstructure and a matte surface having micropeaks with a height not greater than about 150 microinches; (c) passing the base foil and electrolyte from the first electrodeposition zone to a second electrodeposition zone; and (d) passing a direct electric current through the electrolyte from a secondary anode to the cathode spaced from the secondary anode under second mass transfer conditions including a second current density greater than the first current density and which provide a mass transfer poorer than that in the first electrodeposition zone, while introducing into the second electrodeposition zone a supplemental stream of the electrolyte, to electrodeposit on the matte surface micronodules of copper, so as to produce a copper foil having a total matte height not greater than about 200 microinches.
Claim 2
Dependent Claim
245 words
An electrolytic process for producing copper foil having a low profile surface exhibiting a high peel strength when bonded to a polymeric substrate, which process comprises: (a) preparing an electrolyte comprising a copper sulfate-sulfuric acid solution, said solution having added thereto minor amounts of a low molecular weight water-soluble cellulose ether, a low molecular weight water-soluble polyalkylene glycol ether, a low molecular weight water-soluble polyethyleneimine and a water-soluble sulfonated organic sulfur compound; (b) passing a direct electric current through the electrolyte from a primary anode to a cathode spaced from the primary anode in a first electrodeposition zone under first mass transfer conditions including a first current density to electrodeposit on the cathode a base copper foil having a fine-grained microstructure and a matte surface having micropeaks with a height not greater than about 150 microinches; (c) passing the base foil and electrolyte from the first electrodeposition zone to a second electrodeposition zone; and (d) passing a direct electric current through the electrolyte from a secondary anode to the cathode spaced from the secondary anode under second mass transfer conditions including a second current density greater than the first current density and which provide a mass transfer poorer than that in the first electrodeposition zone, while introducing into the second electrodeposition zone a supplemental stream of the electrolyte, to electrodeposit on the matte surface micronodules of copper, so as to produce a copper foil having a total matte height not greater than about 200 microinches.
Claim 3
Dependent Claim
80 words
The process of claim 1, wherein the cathode is a rotating drum immersed in the electrolyte, the electrolyte is supplied from below the cathode and introduced into a first gap between the cathode and the primary anode, the secondary anode is positioned above the primary anode at an exit end and spaced from the cathode, the supplemental electrolyte is introduced into a second gap between an upper end of the primary anode and a lower end of the secondary anode.
Claim 4
Dependent Claim
38 words
The process of claim 2, wherein the electrolyte is fed into the first gap at a rate of about 50-200 l/min; and the supplemental electrolyte is fed into the second gap at a rate of about 20-100 l/min.
Claim 5
Dependent Claim
16 words
A copper-clad laminate comprising the copper foil defined by claim 3 laminated to a polymeric substrate.
Claim 6
Dependent Claim
25 words
The process of claim 3, wherein the first current density is 20-100 A/DCM 2 , and the second current density is 100-300 A/DCM 2 .
Claim 7
Dependent Claim
71 words
The process of claim 5, wherein the fresh electrolyte is formed by adding to an aqueous copper sulfate-sulfuric acid solution an aqueous addition agent stock solution containing the following addition agents: 2-10 g/l hydroxyethyl cellulose; 0.2-1 g/l polyethylene amine; 0.1-1 g/l polyethylene glycol ether; and 0.1-0.5 g/l 2-mercaptoethane sulfonic acid sodium salt, and the addition agents are added to the copper sulfate-sulfuric acid solution at an addition rate of 200-1000 mg/min.
Claim 8
Dependent Claim
20 words
The process of claim 2, wherein the electrolyte in the first gap is agitated by oxygen evolved from the electrolyte.
Claim 9
Dependent Claim
38 words
The process of claim 1, wherein the electrolyte comprises: 60-110 g/l copper; 40-150 g/l H 2 SO 4 ; 2-10 g/l cellulose ether; 0.2-1.0 g/l polyalkylene glycol ether; 0.2-1.0 g/l polyethyleneimine; and 0.1-0.5 g/l sulfonated organic sulfur compound.
Claim 10
Dependent Claim
79 words
The process of claim 1, wherein the cellulose ether is a hydroxyethyl cellulose ether, the polyalkylene glycol ether is selected from the group consisting of polyethylene glycol monoethyl and dimethyl ethers; the polyethyleneimine is selected from the group consisting of polyethyleneimines having a molecular weight of from about 250 to 1800; and the sulfonated organic sulfur compounds are selected from the group consisting of aliphatic and aromatic compounds having an average molecular weight of from about 100 to 600.
Claim 11
Dependent Claim
23 words
The process of claim 1, further including applying to the produced foil at least a zinc-containing barrier layer and a chromium-containing stain-proofing layer.
Claim 12
Dependent Claim
32 words
The process of claim 9, wherein the produced foil is passed directly from the second electrodeposition zone to, in sequence, at least a barrier layer applying station and, a stain-proofing applying station.
Claim 13
Dependent Claim
13 words
Copper foil produced by the process defined by any one of claims 1-10.
Claim 14
Dependent Claim
72 words
An electrolytic process for producing copper foil, comprising passing an electric current through an electrolyte from an anode spaced from a cathode to electrodeposit copper foil on the cathode, wherein said electrolyte comprises a copper sulfate-sulfuric acid solution having added thereto minor amounts of a low molecular weight water-soluble cellulose ether, a low molecular weight water-soluble polyethylene glycol ether, a low molecular weight water-soluble polyethyleneimine, and a water-soluble sulfonated organic sulfur compound.
Claim 15
Dependent Claim
72 words
An electrolytic process for producing copper foil, comprising passing an electric current through an electrolyte from an anode spaced from a cathode to electrodeposit copper foil on the cathode, wherein said electrolyte comprises a copper sulfate-sulfuric acid solution having added thereto minor amounts of a low molecular weight water-soluble cellulose ether, a low molecular weight water-soluble polyethylene glycol ether, a low molecular weight water-soluble polyethyleneimine, and a water-soluble sulfonated organic sulfur compound.
References Cited (Backward Citations)
US3674656A
Cited
US3857681A
Cited
US4572768A
Cited
WO1987003915A1
Cited
US5433840A
Cited
US5215646A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 2002-01-25 | 2002-07-27 | 2003-01-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2006-01-25 | 2006-07-27 | 2007-01-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2010-01-25 | 2010-07-27 | 2011-01-26 | $7700.00 | Window Closed / Lapsed |