US2321182A - Electrodeposition of nickel from an acid bath - Google Patents

Electrodeposition of nickel from an acid bath Download PDF

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US2321182A
US2321182A US287057A US28705739A US2321182A US 2321182 A US2321182 A US 2321182A US 287057 A US287057 A US 287057A US 28705739 A US28705739 A US 28705739A US 2321182 A US2321182 A US 2321182A
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nickel
solution
group
aldehyde
electrodepositing
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US287057A
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Brown Henry
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Udylite Corp
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Udylite Corp
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    • 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

Description

Patented June 8, 1943 ELECTRODEPOSITION OF NICKEL FROM AN (ID BATH Henry Brown, Detroit, Mich, assignor to The Udylite Corporation, Detroit, Mich, a corporation of Delaware No Drawing. Application July 28, 1939, Serial No. 287,057
13 Claims.
This invention relates to the electro-deposltion of nickel from an acid bath.
It is an object of this invention to produce a fine-grained, lustrous, ductile nickel deposit.
Another object of the invention is to decrease the tendency of the formation of pits in the plate, such pitting being detrimental from the standpoint of both appearance and corrosion-resistance afforded by the plate.
These objects are accomplished by the addition to a standard nickel sulphate plating bath (commonly called the Watts type nickel plating bath) of certain organic compounds, to wit; halogenated aldehydes. The term halogenated aldehydes as used herein includes not only the halogenated aldehydes but also their hydrates and their acetals, the latter which in water solution regenerate the halogenated aldehydes or bydrates.
This application is a continuation in part of my prior application Serial No. 162,697, filed September '7, 1937.
These halogenated aldehydes, particularly the alpha halogenated aldehydes, have certain definite advantages over the ordinary aldehydes. Several of the ordinary aldehydes are very powerful brighteners, for example, furfural, croton aldehyde, and acrolein. These powerful aldehydes, however, tend to resinify in the plating bath and form products which adversely affect both bond and brightness. The alpha halogenated aldehydes are equally or more powerful brighteners and do not resinify in the warm acid bath. Consequently, the baths are more stable and require less attention. The baths can be left idle for long periods without the need of purification from resinous materials. Since no harmful products are formed, one does not need constant drag-out to keep the amount of such products within necessary limits.
In general, therefore the substitution of halogens in the alpha position relative to the aldehyde group improves the effectiveness of the compound in the nickel bath. The bright plate range is widened and the ability of smoothing out polishing lines and other imperfections with the plating is greatly increased. The bromine atom is more effective than the chlorine atom except where it decreases the solubility unduly as in tribrom obutyraldehyde hydrate.
The use of air agitation in the baths further increases the efficacy of the halogenated aldehydes more so than with ordinary aldehydes.
A number of compounds containing the desired group are listed in Table 1 in the order of their decreasing effectiveness and with their optimum concentrations in baths at 50 C. prepared from nickel sulphate, nickel chloride and boric acid and containing 60'75 grams per liter Ni, 15 grams per liter Cl, 30-375 grams per liter H3130; and pH=2-6 and at a current density of 1 to 5 amp/sq. dm. The temperature of the plating solution can range from 15 C. to the boiling point of the solution. The optimum temperature of the solution when plating, is between 15 C. and 55 C. The preferred temperature of the solution is about 50 C. The solution has better throwing power at lower temperatures and higher pH values than at higher temperatures and lower pH values. The optimum pH- falls between 4 and 5.3 electrometric.
Table 1 Opt. come. all
a Brom, fl clilor, crotonaldehyde hydrate,
ClI3.CC1=CBr-CHO.H20 0.1-0.2
a Chlor, B chlor, crotonaldehyde hydrate,
CH;.CC1=CC1.CHO.HO 0.1-0.2
aa, Dibrom, B mono chlor butyraldehyde hydrate,
drate), CH3.CHC|.CC]2.CHO.H:O 0. 2-1. 25 aafl, Tribromobutyraldehyde hydrate (butyl bromal hy- (irate), CHJ.CI]BT.CBT2.0HO.H2O 0.1- .4 Bromal hydrate, CBmCHOIhO l- .7
p-Proprionchloral hydrate brom benzenesulphonic acid,
llOrS-OOHCLCCl1.Cll0.Ilz0 ;34.0
p-l'roprionchloi'al hydrate benzene sulphonic acid,
1l aS-C 'CHCLC(Jl .ClI ).liz() .:i--'4.o
p-Butyl chloral hydrate benzene sulphonic acid,
ll (MS-O C1l2.Cl1 (11.(1 C]I-C}IO.]]20. .34. U
" Chloral hydrate, (7 (311.011 0.11:0 0. 5-1. 5
Chloral social, 0 Ch.C=(0 C2115): 0. -2. 0
Mixtures of two or more aldehydes widens the plating range. Desirable mixtures include: .3 g./l. bromal hydrate and 1 g./l. butyl chloral hydrate; .5 g./l. chloral hydrate and .4 g./l. dibrommonochlorbutyraldehyde hydrate; 1 g./l. butyl chloral hydrate and 2 ml./l. formaldehyde (40% solution). 4
The concentration of the halogenated aldehydes should not be allowed to increase above the upper limit of the optimum concentration. as larger quantities tend to hurt the adhesion of the nickel coating and the covering power in recesses (now current density areas) I claim: g
l. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of eleetrodepositing nickel from an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickelchloride, and a mixture of nickel chloride and nickel sulphate in the presence of an aliphatic polyhalogenated aldehyde soluble in the solution and having at least one halogen the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
2. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate and having a pH falling within a range from about 2 to about 6 electrometric in the presence of an aliphatic polyhalogenated aldehyde soluble in the solution and having at least one halogen atom in alpha position to the aldehyde group,
A the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
3. 'A method for electrodepositing nickel to obtain a fine-grained deposit comprising the stepof electrodepositing nickel from an aqueous acid? nickel solution comprising essentially a material selected from the group consisting of {nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate and having a pH falling within a range from about 2 to about 6"-,el ectrometric in the presence of an aliphatic polyhalogenated aldehyde soluble in the solution and having a concentration in the solution of at, least .1 gram per liter and having at least one halogen atom in alpha position to the aldehyde group, the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
4. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution containing boric acid, nickel sulphate and nickel chloride in the presence or an aliphatic polyhalogenated aldehyde soluble in the solution and having at least one halogen atom in alpha position to the aldehyde group, the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
5. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution containing boric acid, nickel sulphate and nickel chloride having a pH falling within a range from about 2 to about 6 electrometric in the presence of an aliphatic polyhalogenated aldehyde soluble in the solution and having at least one halogen atom in alpha position to the aldehyde group, the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
6. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution containing boric acid, nickel suiphate and nickel chloride having a pH falling within a range from about 2 to about 6 electrometric in the presence of an aliphatic polyhalogenated aldehyde soluble in the solution and having a concentration in the solution of at least .1 gram per liter and having at least one halogen atom in alpha position to the aidehyde group, the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
7. A bath for electrodepositing nickel to obatom in alpha position to the aldehyde group,
tain a fine-grained deposit comprising an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate containing an aliphatic polyhalogenated aldehyde soluble in the solution and having at least one halogen atom in alpha position to the aldehyde group, the halogen substituents oi the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
8. A bath for electrodepositing nickel to obtain a fine-grained deposit comprising an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate and having a pH falling within a range from about 2 to about 6 electrometric containing an aliphatic polyhalogenated aldehyde soluble in the solution andhaving at least one halogen atom in alpha position to the aldehyde group, the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
9. A bath for electrodepositing nickel to obtain a fine-grained deposit comprising an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate and having a pH falling within a range from about 2 to about 6 electrometric containing an aliphatic polyhalogenated aldehyde soluble in the solution and having a concentration in the solution of at least .1 gram per liter and having at least one halogen atom in alpha position to the aldehyde group, the halogen substituents of the polyhalogenated aldehyde being selected from the group consisting of chlorine and bromine.
10. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate in the presence of chloral hydrate.
11. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate in the presence of bromal hydrate.
12. A method for electrodepositing nickel to obtain a fine-grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate in the presence of butyl chloral hydrate.
13. A method for electrodepositing nickel to obtain a fine grained deposit comprising the step of electrodepositing nickel from an aqueous acid nickel solution comprising essentially a material selected from the group consisting of nickel sulphate, nickel chloride, and a mixture of nickel chloride and nickel sulphate and containing chloral hydrate in an amount not greater than 1.5 grams per liter of solution.
HENRY BROWN.
US287057A 1939-07-28 1939-07-28 Electrodeposition of nickel from an acid bath Expired - Lifetime US2321182A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2534911A (en) * 1948-04-03 1950-12-19 Houdaille Hershey Corp Process of removing hydrogen embrittlement of bright nickel electrodeposits
US2900707A (en) * 1954-08-06 1959-08-25 Udylite Corp Metallic protective coating

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2534911A (en) * 1948-04-03 1950-12-19 Houdaille Hershey Corp Process of removing hydrogen embrittlement of bright nickel electrodeposits
US2900707A (en) * 1954-08-06 1959-08-25 Udylite Corp Metallic protective coating

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