[go: up one dir, main page]

US3898138A - Method and bath for the electrodeposition of nickel - Google Patents

Method and bath for the electrodeposition of nickel Download PDF

Info

Publication number
US3898138A
US3898138A US515130A US51513074A US3898138A US 3898138 A US3898138 A US 3898138A US 515130 A US515130 A US 515130A US 51513074 A US51513074 A US 51513074A US 3898138 A US3898138 A US 3898138A
Authority
US
United States
Prior art keywords
nickel
per liter
diol
grams per
bath
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US515130A
Inventor
Richard J Clauss
Roy W Klein
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
OMI International Corp
Original Assignee
Oxy Metal Industries Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Oxy Metal Industries Corp filed Critical Oxy Metal Industries Corp
Priority to US515130A priority Critical patent/US3898138A/en
Priority to CA219,108A priority patent/CA1045578A/en
Priority to DE2505499A priority patent/DE2505499C2/en
Priority to FR7504079A priority patent/FR2288163A1/en
Priority to AU78178/75A priority patent/AU484928B2/en
Priority to JP50021396A priority patent/JPS5823477B2/en
Priority to IT48268/75A priority patent/IT1029808B/en
Priority to NL7502531A priority patent/NL7502531A/en
Priority to AR258478A priority patent/AR210076A1/en
Priority to BR3346/75A priority patent/BR7502634A/en
Priority to GB22316/75A priority patent/GB1484227A/en
Application granted granted Critical
Publication of US3898138A publication Critical patent/US3898138A/en
Assigned to HOOKER CHEMICALS & PLASTICS CORP. reassignment HOOKER CHEMICALS & PLASTICS CORP. MERGER (SEE DOCUMENT FOR DETAILS). Assignors: OXY METAL INDUSTRIES CORPORATION
Assigned to OCCIDENTAL CHEMICAL CORPORATION reassignment OCCIDENTAL CHEMICAL CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). EFFECTIVE MARCH 30, 1982. Assignors: HOOKER CHEMICAS & PLASTICS CORP.
Assigned to OMI INTERNATIONAL CORPORATION reassignment OMI INTERNATIONAL CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: OCCIDENTAL CHEMICAL CORPORATION
Assigned to MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF reassignment MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: INTERNATIONAL CORPORATION, A CORP OF DE
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/12Electroplating: Baths therefor from solutions of nickel or cobalt

Definitions

  • metasulfobenzoic acid or its salts are (1) metasulfobenzoic acid or its salts; (2) butynediol or hexyne diol; and (3) butene diol and butenol alcohols.
  • Aldehydesy such as chloral hydrate and formaldehyde, may be added to assist in grain refinement and in reducing the sulfur content of the bath.
  • nickel bromide and nickel chloride The nickel salts are present in amounts conventional in the art, e.g., up to about 100 grams per liter of NiCl .6I-I O).
  • the patent discloses the addition to such baths of a specific aryl sulfon compound, namely metasulfobenzoic acid or its derivatives, such as Ni-carboxy benzene sulfonic acid can be utilized.
  • aldehyde such as chloral hydrate or formaldehyde
  • An aldehyde may be added to the patented bath for grain refinement and to reduce the sulfur content of the bath.
  • the general purpose of nickel electroplating is to yield a semi-bright deposit having the desirable characteristics of ductility, uniformly fine grained appearance, and good leveling characteristics. Normally, these objectives are met by the use of coumarin and other additives.
  • the deposit from a nickel solution containing coumarin generally deteriorates during use due to the gradual accumulation of the degradation products of the coumarin itself. These degradation products, such as melilotic acid and related compounds, are detrimental to the leveling and ductility of the deposit. As a result, these deposits must be removed by batch carbon treatments at periodic intervals, adding to the expense of the operation and normally resulting in time consuming, shortened scheduled production runs.
  • the present invention utilizes a specific combination of compounds which results in nickel deposits which are fine grained, lustrous, and ductile and which have markedly improved leveling characteristics. Although the leveling characteristics of the bath of the present invention are not quite as good as those obtained through the use of coumarin, the present invention does permit continuous use of the nickel solution without the accumulation of those deleterious degradation products which are developed in coumarin solutions.
  • the deposits from the solutions of the present invention generally contain less than about 0.005% sulfur.
  • the present invention is directed to the addition to baths such as those defined in U.S. Pat. No. 3,264,200 of a combination of three specific compositions or compounds.
  • the nickel-containing and pl-l-controlling elements of the bath are conventional and may be of any desired type, as defined in the noted patent.
  • the bath of the present invention may be of the Watts or modified Watts type containing nickel sulfate; of the sulfamate type; of the nickel fluoborate type; of the nickel bromide type; or of the nickel chloride type.
  • the pH of the bath is controlled by the use of boric acid (H 30 and an aldehyde, such as formaldehyde and/or chloral hydrate may be added, as above explained.
  • boric acid H 30 and an aldehyde, such as formaldehyde and/or chloral hydrate may be added, as above explained.
  • alkyne diol specifically butyne diol (l-IOH CC 5 CCH OH) or 3-l-Iexyne 2, 5 diol CH CH(OH)C 2 CCH(OH) CH being present in an amount ranging from about 0.05 to about 0.5 grams per liter of the bath; and
  • an important object of the present invention to provide a bath for the electrodeposition of nickel plate from an aqueous acidic nickel plating bath containing dissolved therein an aryl sulfon, an alkyne diol and a short chain alkene alcohol.
  • Another important object of the present invention is the provision of a method of electrodeposition of duetile, low-stress nickel plate having good leveling characteristics and including the step of electrodepositing semi-bright ductile nickel from an aqueous acidic nickel plating bath containing metasulfobenzoic acid or its salts, and a combination of at least one alkyne diol and at least one alkene alcohol containing four carbon atoms.
  • Another object of the present invention is the provision of a method of electrodepositing ductile low-stress nickel plate from an aqueous acidic nickel plating bath containing at least one nickel salt and metasulfobenzoic acid or its salts, residing in the improvement of incorporating in the bath a mixture of an alkene diol selected from the group consisting of butyne diol and hexyne diol, and an alkene alcohol selected from the group consisting of butene diol, butenol, and isomeric forms of butenol.
  • the present invention constitutes an improvement upon the invention disclosed and claimed in US. Pat. No. 3,264,200, assigned to the assignee of the present invention.
  • This improvement resides in the discovery of the synergistic effect which can be obtained from the incorporation of a specific mixture of specific unsaturated alcohols into the aqueous acidic nickel plating baths proposed in said earlier patent.
  • the earlier patent proposes the incorporation of metasulfobenzoic acid or the nickel salt of the compound into a bath for the electrodeposition of ductile, semibright nickel plate.
  • the mentioned patent discloses the incorporation of from 0.1 to about 10 grams per liter of metasulfobenzoic acid.
  • the metasulfobenzoic acid is usually neutralized with nickel hydroxide or nickel carbonate and is added to the bath as a nickel salt. It, however, can be added as the free acid, or as sodium or magnesium salt. If too high a concentration of the free acid is added to the nickel bath at one time, the pH of the bath will be substantially reduced. Therefore, the nickel salt of the acid is the preferred form, where additions of concentrations greater than about one gram per liter are added at one time. It should be understood that when metasulfobenzoic acid is referred to herein, this expression includes the nickel salt of the compound. Even where the free acid is added to the nickel bath, the metasulfobenzoic acid is generally in the form of the nickel salt, or the ionized nickel salt.
  • the acetylenic diols which are added are preferably in the simple unreacted diol form, since it has been found that the derivatives thereof, such as the epichlorohydrin adduct of butyne diol are not very effective.
  • the two preferred alkyne diols are butyne 1, 4 diol, HOCH CC CCH OH or 3-hexyne 2, 5 diol CH CH(OI-I)C E CCI-I(OH)CH This ingredient is added in an amount ranging from about 0.05 to about 0.5 grams per liter of the solution. Short chained alkene alcohols are used in conjunction with the alkyne diols.
  • the alkene alcohols uniformly contain four carbon atoms and, as above noted, are effective whereas other specific unsaturated alcohols do not work in the combination, for example, allyl alcohol (CI-I :CI-ICH Ol-I) is ineffective.
  • concentration of the alkyne alcohol and the concentration of the alkene alcohol is defined as falling within the same broad range. It has been found that it is not necessary to use equal amounts of the two compounds, nor is the utilization of a specific combination of compounds within a defined group essential.
  • any suitable type of semi-bright nickel plating bath can be utilized, and the herein disclosed, three component combination is effective in sulfamate, fluoborate, bromide, and low chloride (less than 100 grams per liter NiC1 .6H O) baths.
  • the preferred pH range is from about 2.8 to about 4.5, and the preferred bath temperature may range from 130 to 140F.
  • the cathode current density may be an average of 40 to 60 amps per square foot with air agitation.
  • the Examples yielded lustrous, ductile, very low-stressed semi-bright nickel deposits which contain less than about 0.005% sulfur, and which have remarkedly good leveling characteristics.
  • the deposit which was obtained had improved leveling characteristics over the corresponding baths of US. Pat. No. 3,264,200.
  • a bath for the electrodeposition of ductile, lowstress nickel plate from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride, and containing dissolved therein from about 01 to about grams per liter of metsulfobenzoic acid, from about 0.05 to about 0.5 grams per liter of an alkyne diol selected from the group consisting of butyne diol and hexyne diol, and from about 0.05 to about 0.5- grams per liter of an alkene alcohol selected from the group consisting of butene diol, butenol and isomers of buteno].
  • a bath for the electrodeposition of ductile low- Ill stress nickel plate from an aqueous acidic nickel plating bath said bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride and containing dissolved therein from about 0.1 to about 10 grams per liter of metasulfobenzoic acid, the improvement of incorporating into said bath a combination of from about 0.05 to about 0.5 grams per liter of an alkyne diol and from about 0.05 to about 0.5 grams per liter of a butene alcohol.
  • a method for the electrodeposition of ductle lowstress nickel plate exhibiting improved leveling characteristics comprising the step of electrodepositing semibright ductile nickel from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride and having dissolved therein from about 0.1 to about 10 grams per liter of metasulfobenzoic acid, from about 0.05 to about 0.5 grams per liter of an alkyne diol selected from the group consisting of butyne diol and hexyne diol, and from about 0.05 to about 0.5 grams per liter of an alkene alcohol selected from the group consisting of butyne diol, butenol and isomers of butenol.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating And Plating Baths Therefor (AREA)

Abstract

This invention relates to an improvement in the plating of ductile semi-bright nickel from aqueous acidic nickel electroplating solutions, by the addition of three conjunctive ingredients, i.e., an aryl sulfon, an acetylenic alcohol and an olefinic alcohol. The conjunctive use of these three types of compounds produce excellent semi-bright nickel deposits which are ductile, finegrained and which exhibit improved leveling characteristics. Specific compounds which can be utilized are (1) metasulfobenzoic acid or its salts; (2) butynediol or hexyne diol; and (3) butene diol and butenol alcohols. Aldehydes, such as chloral hydrate and formaldehyde, may be added to assist in grain refinement and in reducing the sulfur content of the bath.

Description

United States Patent Clauss et a1.
[451 Aug. 5, 1975 METHOD AND BATH FOR THE ELECTRODEPOSITION OF NICKEL [75] Inventors: Richard J. Clauss, Allen Park; Roy
W. Klein, St. Clair Shores, both of Mich.
[73] Assignee: Oxy Metal Industries Corporation,
Warren, Mich.
221 Filed: on. 16,1974
211 App]. No.:515,l30
[52] U.S. Cl. 204/49 [51] Int. Cl. C23b 5/08; C23b 5/46 [58] Field of Search 204/49, 43 T, 43 N, 43 P,
[56] References Cited UNITED STATES PATENTS 3,264,200 8/1966 Clauss et al 204/49 Primary ExaminerG. L. Kaplan Attorney, Agent, or Firm-B. F. Claeboe 57 1 ABSTRACT This invention relates to an improvement in the plating of ductile semi-bright nickel from aqueous acidic nickel electroplating solutions, by the addition of three conjunctive ingredients, i.e., an aryl sulfon, an acetylenic alcohol and an olefinic alcohol. The conjunctive use of these three types of compounds produce excellent semi-bright nickel deposits which are ductile, finegrained and which exhibit improved leveling characteristics. Specific compounds which can be utilized are (1) metasulfobenzoic acid or its salts; (2) butynediol or hexyne diol; and (3) butene diol and butenol alcohols. Aldehydesysuch as chloral hydrate and formaldehyde, may be added to assist in grain refinement and in reducing the sulfur content of the bath.
4 Claims, N0 Drawings METHOD AND BATH FOR THE ELECTRODEPOSITION OF NICKEL BACKGROUND OF THE INVENTION The present invention constitutes a specific improvement over the invention defined in U.S. Pat, No. 3,264,200 patented Aug. 2, 1966, and assigned to the Assignee of the present invention.
In U.S. Pat. No. 3,264,200, there is disclosed an improved method of and bath for the electrodeposition of ductile, lowstress nickel plate from an aqueous acidic nickel plating bath containing at least one nickel salt, which nickel salt is selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate,
nickel bromide and nickel chloride. The nickel salts are present in amounts conventional in the art, e.g., up to about 100 grams per liter of NiCl .6I-I O). The patent discloses the addition to such baths of a specific aryl sulfon compound, namely metasulfobenzoic acid or its derivatives, such as Ni-carboxy benzene sulfonic acid can be utilized.
An aldehyde, such as chloral hydrate or formaldehyde, may be added to the patented bath for grain refinement and to reduce the sulfur content of the bath.
The general purpose of nickel electroplating, of course, is to yield a semi-bright deposit having the desirable characteristics of ductility, uniformly fine grained appearance, and good leveling characteristics. Normally, these objectives are met by the use of coumarin and other additives. However, the deposit from a nickel solution containing coumarin generally deteriorates during use due to the gradual accumulation of the degradation products of the coumarin itself. These degradation products, such as melilotic acid and related compounds, are detrimental to the leveling and ductility of the deposit. As a result, these deposits must be removed by batch carbon treatments at periodic intervals, adding to the expense of the operation and normally resulting in time consuming, shortened scheduled production runs.
The bath of U.S. Pat. No. 3,264,200 was developed to reduce the problems encountered in the accumulation of coumarin degradation products. Generally, a bath containing metasulfobenzoic acid and its derivatives, particularly wherein aldehydes are incorporated, gives a fine lustrous nickel deposit which is ductile and of fine grained appearance. However, the leveling characteristics are substantially reduced. The presence of the aldehydes also appears to detract from the leveling characteristics of the nickel deposit.
If it were possible to develop a process and bath which is free of coumarin, thereby avoiding the accmulation of the coumarin degradation products, yet which yields the excellent leveling characteristics of coumarin-containing baths, an important forward step in the art of nickel electrodeposition could be made.
BRIEF SUMMARY OF THE PRESENT INVENTION The present invention utilizes a specific combination of compounds which results in nickel deposits which are fine grained, lustrous, and ductile and which have markedly improved leveling characteristics. Although the leveling characteristics of the bath of the present invention are not quite as good as those obtained through the use of coumarin, the present invention does permit continuous use of the nickel solution without the accumulation of those deleterious degradation products which are developed in coumarin solutions. The deposits from the solutions of the present invention generally contain less than about 0.005% sulfur.
More specifically, the present invention is directed to the addition to baths such as those defined in U.S. Pat. No. 3,264,200 of a combination of three specific compositions or compounds. The nickel-containing and pl-l-controlling elements of the bath are conventional and may be of any desired type, as defined in the noted patent.
The bath of the present invention may be of the Watts or modified Watts type containing nickel sulfate; of the sulfamate type; of the nickel fluoborate type; of the nickel bromide type; or of the nickel chloride type.
The pH of the bath is controlled by the use of boric acid (H 30 and an aldehyde, such as formaldehyde and/or chloral hydrate may be added, as above explained.
The specific addition agents of the present invention have a conjunctive affect and are used in combination. Specifically, these three ingredients include:
1. An aryl sulfon, specifically metsulfobenzoic acid or its nickel salts such as Ni-carboxy benzene sulfonic acid. This ingredient is present in an amount ranging from about 0.1 to about 10 grams per liter of the bath.
2. An alkyne diol, specifically butyne diol (l-IOH CC 5 CCH OH) or 3-l-Iexyne 2, 5 diol CH CH(OH)C 2 CCH(OH) CH being present in an amount ranging from about 0.05 to about 0.5 grams per liter of the bath; and
3. A butene alcohol, specifically butene diol (HOCl-l CI-l:CHCH Ol-I) or butenol (Cl-I CH:CHCH OH) or isomers of butenol, i.e. either 3 butene-l-ol H C=CHCH CH OH or 3 butene- 2-ol-H C=CHCH(OH )CH this ingredient also being present in an amount ranging from about 0.05 to about 0.5 grams per liter of the bath.
It has been found that these three ingredients, used in conjunction with one another, exert a synergistic affect upon the bath in which they are incorporated so that the bath yields a nickel deposit which is semibright, ductile, of low-stress and of remarkably good leveling characteristics, the deposit generally containing a maximum sulfur content of about 0.005 percent, and the bath remaining free of those decomposition products, commonly encountered in the use of coumarin as a bath ingredient.
It is, therefore, an important object of the present invention to provide a bath for the electrodeposition of nickel plate from an aqueous acidic nickel plating bath containing dissolved therein an aryl sulfon, an alkyne diol and a short chain alkene alcohol.
Another important object of the present invention is the provision of a method of electrodeposition of duetile, low-stress nickel plate having good leveling characteristics and including the step of electrodepositing semi-bright ductile nickel from an aqueous acidic nickel plating bath containing metasulfobenzoic acid or its salts, and a combination of at least one alkyne diol and at least one alkene alcohol containing four carbon atoms.
It is a further important object of the present invention to provide an aqueous, nickel salt containing bath for the electrodeposition of semi-bright nickel plate and having incorporated therein from about 0.1 to about grams per liter of metasulfobenzoic acid or its nickel salts, from about 0.05 to about 0.5 grams per liter of an alkyne diol selected from the group consisting of butyne diol and hexyne diol, and from about 0.05 to about 0.5 grams per liter of an alkene alcohol selected from the group consisting of butene diol, butenol and isomeric forms of butenol.
Another object of the present invention is the provision of a method of electrodepositing ductile low-stress nickel plate from an aqueous acidic nickel plating bath containing at least one nickel salt and metasulfobenzoic acid or its salts, residing in the improvement of incorporating in the bath a mixture of an alkene diol selected from the group consisting of butyne diol and hexyne diol, and an alkene alcohol selected from the group consisting of butene diol, butenol, and isomeric forms of butenol.
DETAILED DESCRIPTION OF THE PRESENT INVENTION As above explained, the present invention constitutes an improvement upon the invention disclosed and claimed in US. Pat. No. 3,264,200, assigned to the assignee of the present invention. This improvement resides in the discovery of the synergistic effect which can be obtained from the incorporation of a specific mixture of specific unsaturated alcohols into the aqueous acidic nickel plating baths proposed in said earlier patent.
More specifically, the earlier patent proposes the incorporation of metasulfobenzoic acid or the nickel salt of the compound into a bath for the electrodeposition of ductile, semibright nickel plate. To reduce the internal tensile stress of nickel deposits, particularly those deposits obtained from Watts type and sulfamate type acidic nickel electroplating baths, the mentioned patent discloses the incorporation of from 0.1 to about 10 grams per liter of metasulfobenzoic acid.
Various other additions are proposed in the patent, particularly the addition of formaldehyde or chloral hydrate to the bath to assist in giving uniform grain refinement and low sulfur content. Additional additives are also disclosed, including the suggestion that other unsaturated compounds such as allyl alcohol and butyne diol may be added. It has now been determined that the addition of a combination of allyl alcohol and butyne diol is not completely effective to produce the desired and improved leveling characteristicsof the present invention. Rather, the present invention is more particularly concerned with the conjunctive use of a combination of three specific compounds, namely the metasulfobenzoic acid which is the primary additive of US.
Pat. No. 3,364,200, and a mixture of an acetylenic a1- cohol and an alkene alcohol containing four carbon atoms.
As is explained in US. Pat. No. 3,264,200, the metasulfobenzoic acid is usually neutralized with nickel hydroxide or nickel carbonate and is added to the bath as a nickel salt. It, however, can be added as the free acid, or as sodium or magnesium salt. If too high a concentration of the free acid is added to the nickel bath at one time, the pH of the bath will be substantially reduced. Therefore, the nickel salt of the acid is the preferred form, where additions of concentrations greater than about one gram per liter are added at one time. It should be understood that when metasulfobenzoic acid is referred to herein, this expression includes the nickel salt of the compound. Even where the free acid is added to the nickel bath, the metasulfobenzoic acid is generally in the form of the nickel salt, or the ionized nickel salt.
The acetylenic diols which are added are preferably in the simple unreacted diol form, since it has been found that the derivatives thereof, such as the epichlorohydrin adduct of butyne diol are not very effective. The two preferred alkyne diols are butyne 1, 4 diol, HOCH CC CCH OH or 3-hexyne 2, 5 diol CH CH(OI-I)C E CCI-I(OH)CH This ingredient is added in an amount ranging from about 0.05 to about 0.5 grams per liter of the solution. Short chained alkene alcohols are used in conjunction with the alkyne diols. Specific examples include butene diol, (HOCI-I CH:CHCI-I OI-I), butenol, (CI-I CH:CHCH OH) or the isomeric forms of butenol including 3-butene-2ol, CH CHOI-ICH:CI-I or 3 butene-l-ol, (H C=Cl-ICH CH OI-I). The alkene alcohols uniformly contain four carbon atoms and, as above noted, are effective whereas other specific unsaturated alcohols do not work in the combination, for example, allyl alcohol (CI-I :CI-ICH Ol-I) is ineffective.
It will be noted that the concentration of the alkyne alcohol and the concentration of the alkene alcohol is defined as falling within the same broad range. It has been found that it is not necessary to use equal amounts of the two compounds, nor is the utilization of a specific combination of compounds within a defined group essential.
If desired, any suitable type of semi-bright nickel plating bath can be utilized, and the herein disclosed, three component combination is effective in sulfamate, fluoborate, bromide, and low chloride (less than 100 grams per liter NiC1 .6H O) baths.
The following specific examples are submitted:
EXAMPLE I Concentration NiSO .6I-I O 200-300 g/l NiCl .6H O 15-50 g/l H 3050 g/l Meta sulfobenzoic acid (Na salt) 0.2- 5 g/l Chloral hydrate 0.03-0.2 g/l Formaldehyde 0.0l0.l g/l Butyne diol 0.05-0.5 g/l Butene diol 0.05-0.5 g/l EXAMPLE II NiSO .6H O 200-300 g/] NiC1 .6H O 1 550 g/l H 80 30-50 g/l Ni-carboxy benzene l2 g/l sulfonic acid Butyne diol 50-150 mg/l Bulene diol -300 mg/l EXAMPLE III Ni(SO NH y (nickel sulfamate) 250-500 g/l NIC zHz 0-30 g/l H 80 30-50 g/l Butyne diol 75 mg/l Butene diol mg/l Meta sulfobenzoic acid (Na salt) 15 g/l EXAMPLE IV Concentration NiSO .6l-l O 200400 g/l NiCl,.6H O 30-60 g/l Hexyne diol 150 mgll Butene diol 150 mg/l Meta sulfobenzoic ucid (Na salt) 2 g/l The substitution of butenol, 3-butene-2ol, or 3- butene-l-ol for butene diol in Example ll gave equivalent results.
In the above cited Examples, the preferred pH range is from about 2.8 to about 4.5, and the preferred bath temperature may range from 130 to 140F. The cathode current density may be an average of 40 to 60 amps per square foot with air agitation.
In each instance, the Examples yielded lustrous, ductile, very low-stressed semi-bright nickel deposits which contain less than about 0.005% sulfur, and which have remarkedly good leveling characteristics. In each instance, the deposit which was obtained had improved leveling characteristics over the corresponding baths of US. Pat. No. 3,264,200.
What is claimed is:
l. A bath for the electrodeposition of ductile, lowstress nickel plate from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride, and containing dissolved therein from about 01 to about grams per liter of metsulfobenzoic acid, from about 0.05 to about 0.5 grams per liter of an alkyne diol selected from the group consisting of butyne diol and hexyne diol, and from about 0.05 to about 0.5- grams per liter of an alkene alcohol selected from the group consisting of butene diol, butenol and isomers of buteno].
2. In a bath for the electrodeposition of ductile low- Ill stress nickel plate from an aqueous acidic nickel plating bath, said bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride and containing dissolved therein from about 0.1 to about 10 grams per liter of metasulfobenzoic acid, the improvement of incorporating into said bath a combination of from about 0.05 to about 0.5 grams per liter of an alkyne diol and from about 0.05 to about 0.5 grams per liter of a butene alcohol.
3. A method for the electrodeposition of ductle lowstress nickel plate exhibiting improved leveling characteristics comprising the step of electrodepositing semibright ductile nickel from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride and having dissolved therein from about 0.1 to about 10 grams per liter of metasulfobenzoic acid, from about 0.05 to about 0.5 grams per liter of an alkyne diol selected from the group consisting of butyne diol and hexyne diol, and from about 0.05 to about 0.5 grams per liter of an alkene alcohol selected from the group consisting of butyne diol, butenol and isomers of butenol.
4. In a method for the electrodeposition of ductile semi-bright nickel plate of low stress wherein semibright ductile nickel is electrodeposited from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride and containing dissolved therein from about 0.1 to about 10 grams per liter of metasulfobenzoic acid, the improvement yielding improved leveling characteristics of incorporating into the bath from 0.05 to 0.5 grams per liter of an alkyne diol, and from 0.05 to 0.05 grams per liter of a butene alcohol.

Claims (4)

1. A bath for the electrodeposition of ductile, lowstress nickel plate from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloriDe, and containing dissolved therein from about 0.1 to about 10 grams per liter of metsulfobenzoic acid, from about 0.05 to about 0.5 grams per liter of an alkyne diol selected from the group consisting of butyne diol and hexyne diol, and from about 0.05 to about 0.5 grams per liter of an alkene alcohol selected from the group consisting of butene diol, butenol and isomers of butenol.
2. IN A BATH FOR THE ELECTRODEPOSITION OF DUCTILE LOW-STRESS NICKEL PLATE FROM AN AQUEOUS ACIDIC NICKEL PLATING BATH SAID BATH CONTAINING AT LEAST ONE NICKEL SAT SELECTED FROM THE GROUP CONTAINING OF NICKEL SULFATE NICKEL SULFAMATE, NICKEL FLUOBORATE NICKEL BROMIDE AND NICKEL CHLORIDE AND CONTAINING DISSOLVED THEREIN FROM ABOUT 0.1 TO ABOUT 10 GRAMS PER LITER OF METASULFOBENZOIC ACID THE IMPROVEMENT IN INCORPORATING INTO SAID BATH A COMBINATION OF FROM ABOUT 0.05 TO ABOUT 0.5 GGRAMS PER LITER OF AN ALKYNE DIOL AND FROM ABOUT 0.05 TO ABOUT 0.5 GRAMS PER LITER OF A BUTENE ALCOHOL.
3. A method for the electrodeposition of ductle low-stress nickel plate exhibiting improved leveling characteristics comprising the step of electrodepositing semi-bright ductile nickel from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride and having dissolved therein from about 0.1 to about 10 grams per liter of metasulfobenzoic acid, from about 0.05 to about 0.5 grams per liter of an alkyne diol selected from the group consisting of butyne diol and hexyne diol, and from about 0.05 to about 0.5 grams per liter of an alkene alcohol selected from the group consisting of butyne diol, butenol and isomers of butenol.
4. In a method for the electrodeposition of ductile semi-bright nickel plate of low stress wherein semi-bright ductile nickel is electrodeposited from an aqueous acidic nickel plating bath containing at least one nickel salt selected from the group consisting of nickel sulfate, nickel sulfamate, nickel fluoborate, nickel bromide and nickel chloride and containing dissolved therein from about 0.1 to about 10 grams per liter of metasulfobenzoic acid, the improvement yielding improved leveling characteristics of incorporating into the bath from 0.05 to 0.5 grams per liter of an alkyne diol, and from 0.05 to 0.05 grams per liter of a butene alcohol.
US515130A 1974-10-16 1974-10-16 Method and bath for the electrodeposition of nickel Expired - Lifetime US3898138A (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
US515130A US3898138A (en) 1974-10-16 1974-10-16 Method and bath for the electrodeposition of nickel
CA219,108A CA1045578A (en) 1974-10-16 1975-01-31 Method and bath for the electrodeposition of nickel
DE2505499A DE2505499C2 (en) 1974-10-16 1975-02-10 Aqueous acid bath for the electrodeposition of ductile nickel
FR7504079A FR2288163A1 (en) 1974-10-16 1975-02-10 DUCTILE NICKEL ELECTROLYTIC DEPOSIT BATHS AND METHODS USING THESE BATHS
AU78178/75A AU484928B2 (en) 1975-02-13 Method and bath forthe electrodeposition of nickel
JP50021396A JPS5823477B2 (en) 1974-10-16 1975-02-20 Nikkeru nodenkitokinhouhou Oyobi Tokinyoku
IT48268/75A IT1029808B (en) 1974-10-16 1975-02-20 BATHROOM AND METHOD TO ELECTROPLACE NICKEL
NL7502531A NL7502531A (en) 1974-10-16 1975-03-04 METHOD FOR THE ELECTROLYTIC DEPOSITION OF NICKEL.
AR258478A AR210076A1 (en) 1974-10-16 1975-04-23 A BATHROOM FOR THE NICKEL PLATED ELECTRODEPOSITION
BR3346/75A BR7502634A (en) 1974-10-16 1975-04-30 BATH FOR ELECTRONOPOSITION OF NICKEL COATING AND PROCESS FOR ELECTRODEPOSITION OF NICKEL COATING
GB22316/75A GB1484227A (en) 1974-10-16 1975-05-22 Method and bath for the electrodeposition of nickel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US515130A US3898138A (en) 1974-10-16 1974-10-16 Method and bath for the electrodeposition of nickel

Publications (1)

Publication Number Publication Date
US3898138A true US3898138A (en) 1975-08-05

Family

ID=24050093

Family Applications (1)

Application Number Title Priority Date Filing Date
US515130A Expired - Lifetime US3898138A (en) 1974-10-16 1974-10-16 Method and bath for the electrodeposition of nickel

Country Status (10)

Country Link
US (1) US3898138A (en)
JP (1) JPS5823477B2 (en)
AR (1) AR210076A1 (en)
BR (1) BR7502634A (en)
CA (1) CA1045578A (en)
DE (1) DE2505499C2 (en)
FR (1) FR2288163A1 (en)
GB (1) GB1484227A (en)
IT (1) IT1029808B (en)
NL (1) NL7502531A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2583070A1 (en) * 1985-06-11 1986-12-12 Limburgs Galvano Tech Bedri Process for protecting steel components, in particular hydraulic cylinders, against wear and corrosion.
US5269838A (en) * 1992-04-20 1993-12-14 Dipsol Chemicals Co., Ltd. Electroless plating solution and plating method with it
EP1300487A1 (en) * 2001-10-02 2003-04-09 Shipley Co. L.L.C. Plating bath and method for depositing a metal layer on a substrate
WO2008154722A1 (en) * 2007-06-18 2008-12-24 Vale Inco Limited Method for improving nickel cathode morphology
US20110155582A1 (en) * 2009-11-18 2011-06-30 Tremmel Robert A Semi-Bright Nickel Plating Bath and Method of Using Same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102014207778B3 (en) * 2014-04-25 2015-05-21 Kiesow Dr. Brinkmann GmbH & Co. KG Use of a mixture for use in a plating bath or plating bath to produce a bright nickel plating, and to a method of making an article having a bright nickel plating

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3264200A (en) * 1964-01-16 1966-08-02 Udylite Corp Electrodeposition of nickel

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1266377A (en) * 1960-09-01 1961-07-07 Metal & Thermit Corp Bright nickel electroplating

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3264200A (en) * 1964-01-16 1966-08-02 Udylite Corp Electrodeposition of nickel

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2583070A1 (en) * 1985-06-11 1986-12-12 Limburgs Galvano Tech Bedri Process for protecting steel components, in particular hydraulic cylinders, against wear and corrosion.
US5269838A (en) * 1992-04-20 1993-12-14 Dipsol Chemicals Co., Ltd. Electroless plating solution and plating method with it
EP1300487A1 (en) * 2001-10-02 2003-04-09 Shipley Co. L.L.C. Plating bath and method for depositing a metal layer on a substrate
US6773573B2 (en) 2001-10-02 2004-08-10 Shipley Company, L.L.C. Plating bath and method for depositing a metal layer on a substrate
WO2008154722A1 (en) * 2007-06-18 2008-12-24 Vale Inco Limited Method for improving nickel cathode morphology
US20110155582A1 (en) * 2009-11-18 2011-06-30 Tremmel Robert A Semi-Bright Nickel Plating Bath and Method of Using Same
WO2012121829A1 (en) * 2011-03-09 2012-09-13 Macdermid Acumen, Inc. Semi-bright nickel plating bath and method of using same
CN103415653A (en) * 2011-03-09 2013-11-27 麦克德米德尖端有限公司 Semi-bright nickel plating bath and method of using same
EP2683853B1 (en) 2011-03-09 2017-10-11 MacDermid Acumen, Inc. Semi-bright nickel plating bath and method of using same

Also Published As

Publication number Publication date
BR7502634A (en) 1976-08-31
NL7502531A (en) 1976-04-21
FR2288163A1 (en) 1976-05-14
JPS5823477B2 (en) 1983-05-16
AR210076A1 (en) 1977-06-30
CA1045578A (en) 1979-01-02
AU7817875A (en) 1976-08-19
DE2505499C2 (en) 1982-01-21
DE2505499A1 (en) 1976-04-29
IT1029808B (en) 1979-03-20
GB1484227A (en) 1977-09-01
JPS5147538A (en) 1976-04-23
FR2288163B1 (en) 1979-06-29

Similar Documents

Publication Publication Date Title
US2436316A (en) Bright alloy plating
CA1051818A (en) Bath and method for the electrodeposition of bright nickel-iron deposits
DE3710368C2 (en)
US3898138A (en) Method and bath for the electrodeposition of nickel
US2658032A (en) Electrodeposition of bright copper-tin alloy
US3862019A (en) Composition of electroplating bath for the electrodeposition of bright nickel
US2550449A (en) Electrodeposition of nickel from an acid bath
US3030282A (en) Electrodeposition of copper
US3140988A (en) Electrodeposition of nickel
US3795592A (en) Nickel electroplating composition and process
US3264200A (en) Electrodeposition of nickel
US2751341A (en) Electrodeposition of lead and lead alloys
US2773022A (en) Electrodeposition from copper electrolytes containing dithiocarbamate addition agents
US2389135A (en) Electrodeposition of metals
US2986500A (en) Electrodeposition of bright nickel
US4089754A (en) Electrodeposition of nickel-iron alloys
US2541700A (en) Electroplating copper
US3697392A (en) Electrodeposition of nickel
US2873234A (en) Electrodeposition of copper
US3663378A (en) Electroplating of nickel
US3401097A (en) Electrodeposition of nickel
US2818376A (en) Nickel plating
US3261772A (en) Nickel electroplating bath and process
US3709798A (en) Electrodeposition of nickel
US3759803A (en) Alkaline nickel plating solutions

Legal Events

Date Code Title Description
AS Assignment

Owner name: HOOKER CHEMICALS & PLASTICS CORP.

Free format text: MERGER;ASSIGNOR:OXY METAL INDUSTRIES CORPORATION;REEL/FRAME:004075/0885

Effective date: 19801222

AS Assignment

Owner name: OCCIDENTAL CHEMICAL CORPORATION

Free format text: CHANGE OF NAME;ASSIGNOR:HOOKER CHEMICAS & PLASTICS CORP.;REEL/FRAME:004126/0054

Effective date: 19820330

AS Assignment

Owner name: OMI INTERNATIONAL CORPORATION, 21441 HOOVER ROAD,

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:OCCIDENTAL CHEMICAL CORPORATION;REEL/FRAME:004190/0827

Effective date: 19830915

AS Assignment

Owner name: MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF NY

Free format text: SECURITY INTEREST;ASSIGNOR:INTERNATIONAL CORPORATION, A CORP OF DE;REEL/FRAME:004201/0733

Effective date: 19830930