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US4541906A Expired / Lapsed US ⏱️ 0.0 years remaining

Zinc electroplating and baths therefore containing carrier brighteners

Assignee: OMI International Corp
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Filing: 1984-05-21
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Granted: 1985-09-17
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Expires: 2004-05-21
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Abstract

Abstract An improved aqueous acidic zinc electrolyte and process for electrodepositing zinc on a conductive substrate in which the electrolyte contains a brightening amount of a bath soluble anionic sulfated polyoxyalkylene surfactant derived from the sulfation of: (a) the polymerization of alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, glycidol, butylene oxide and mixtures thereof; and (b) the alkoxylation of mono and polyhydroxy compounds having radicals selected from the group consisting of hydroxyl containing alkyl, alkenyl, alkynyl, aryl, and carboxylic derivatives thereof as well as mixtures thereof. The zinc electrolyte can further contain conventional additives and agents of the types employed in acid zinc electrolytes to provide modifications and desired characteristics of the zinc electrodeposit.

Inventors

  • 👤 Sylvia Martin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 21:27
CPC Classifications
C; C08; C08G; C08G65/00; C08G65/02; C08G65/32; C08G65/321; C08G65/326; C25; C25D; C25D3/00; C25D3/02; C25D3/22

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 77 words
An aqueous acidic zinc electrolyte containing zinc ions in an amount effective to electrodeposit zinc, hydrogen ions to provide a pH on the acid side, and a brightening amount of a carrier brightener which is a bath soluble anionic sulfated polyoxyalkylene surfactant derived from the sulfation of: the alkoxylation of mono and polyhydroxy compounds having radicals selected from the group consisting of hydroxyl containing alkyl, alkenyl, alkynyl, aryl, and carboxylic derivatives thereof as well as mixtures thereof.
Claim 2
Dependent Claim 77 words
An aqueous acidic zinc electrolyte containing zinc ions in an amount effective to electrodeposit zinc, hydrogen ions to provide a pH on the acid side, and a brightening amount of a carrier brightener which is a bath soluble anionic sulfated polyoxyalkylene surfactant derived from the sulfation of: the alkoxylation of mono and polyhydroxy compounds having radicals selected from the group consisting of hydroxyl containing alkyl, alkenyl, alkynyl, aryl, and carboxylic derivatives thereof as well as mixtures thereof.
Claim 3
Dependent Claim 25 words
The electrolyte as defined in claim 1 in which said sulfated polyoxyalkylene surfactant is present in an amount of about 0.5 to about 20 g/l.
Claim 4
Dependent Claim 25 words
The electrolyte as defined in claim 1 in which said sulfated polyoxyalkylene surfactant is present in an amount of about 2.5 to about 10 g/l.
Claim 5
Dependent Claim 24 words
The electrolyte as defined in claim 1 in which said hydrogen ions are present to provide a pH of about 0 to about 6.
Claim 6
Dependent Claim 24 words
The electrolyte as defined in claim 1 in which said hydrogen ions are present to provide a pH of about 4 to about 5.7.
Claim 7
Dependent Claim 24 words
The electrolyte as defined in claim 1 in which said zinc ions are present in an amount of about 4 g/l up to saturation.
Claim 8
Dependent Claim 28 words
The electrolyte as defined in claim 1 comprising an acid-chloride type in which said zinc ions are present in an amount of about 7 to about 50 g/l.
Claim 9
Dependent Claim 32 words
The electrolyte as defined in claim 1 in which said electrolyte is of the acid-sulfate type and said zinc ions are present in an amount of about 30 to about 110 g/l.
Claim 10
Dependent Claim 23 words
The electrolyte as defined in claim 1 further including primary and/or supplemental brightening agents present in an amount up to about 10 g/l.
Claim 11
Dependent Claim 26 words
The electrolyte as defined in claim 9 in which said primary and/or supplemental brightening agents are present in an amount of at least about 0.001 g/l.
Claim 12
Dependent Claim 26 words
The electrolyte as defined in claim 1 further including primary and/or supplemental brightening agents present in an amount of about 0.01 to about 5 g/l. PG,18
Claim 13
Dependent Claim 20 words
The electrolyte as defined in claim 1 further including conductivity salts present in an amount up to about 450 g/l.
Claim 14
Dependent Claim 148 words
The electrolyte as defined in claim 1 in which said electrolyte is of the acid chloride-type in which said zinc ions are present in an amount of about 15 to about 53 g/l, said hydrogen ions are present to provide a pH of about 4 to about 5.7, said electrolyte further containing conductivity salts present in an amount of about 100 to about 210 g/l, said electrolyte further containing a buffering agent present in an amount of about 15 to about 38 g/l, said sulfated polyoxyalkylene surfactant present in an amount of about 1 to about 5 g/l comprising a compound selected from the group consisting of sulfated 2,4,7,9 tetra-methyl-5-decyne-4,7-diol ethoxylated with 30 mols ethylene oxide, sulfated ethoxylated/propoxylated sorbitol (M.W. 6500), sulfated ethoxylated (15 mols ethylene oxide) β-naphthol, sulfated polyethoxylated lauryl alcohol (about 20 mols ethylene oxide), sulfated polyethoxylated phenol (about 20 mols ethylene oxide), and mixtures thereof.
Claim 15
Dependent Claim 38 words
A process for electrodepositing zinc on a conductive substrate which comprises the steps of contacting a substrate with the aqueous acidic zinc electrolyte as defined in claim 1 and electrodepositing zinc on the substrate to a desired thickness.
Claim 16
Dependent Claim 28 words
A process as defined in claim 14 including the further step of controlling the temperature of the electrolyte within a range of about 60° to about 180° F.
Claim 17
Dependent Claim 28 words
The process as defined in claim 14 including the further step of controlling the temperature of said electrolyte within a range of about 65° to about 90° F.
Claim 18
Dependent Claim 37 words
The process as defined in claim 14 including the further step of controlling the average cathode current density during the step of electrodepositing zinc on the substrate within a range of about 1 to about 300 ASF.
Claim 19
Dependent Claim 46 words
The process as defined in claim 14 in which said electrolyte is of the acid chloride-type including the further step of controlling the average cathode current density during the step of electrodepositing zinc on the substrate within a range of about 1 to about 80 ASF.
Claim 20
Dependent Claim 46 words
The process as defined in claim 14 in which said electrolyte is of the acid sulfate-type including the further step of controlling the average cathode current density during the step of electrodepositing zinc on the substrate within a range of about 20 to about 300 ASF.

References Cited (Backward Citations)

US4089755A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-09-16 1989-03-18 1989-09-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-09-16 1993-03-18 1993-09-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-09-16 1997-03-18 1997-09-17 $7700.00 Window Closed / Lapsed

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