US2523191A - Electrodeposition of nickel from an acid bath - Google Patents

Electrodeposition of nickel from an acid bath Download PDF

Info

Publication number
US2523191A
US2523191A US22489A US2248948A US2523191A US 2523191 A US2523191 A US 2523191A US 22489 A US22489 A US 22489A US 2248948 A US2248948 A US 2248948A US 2523191 A US2523191 A US 2523191A
Authority
US
United States
Prior art keywords
nickel
allyl
mixture
bath
acid
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
US22489A
Inventor
Brown Henry
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.)
Udylite Corp
Original Assignee
Udylite 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
Priority claimed from US603753A external-priority patent/US2523190A/en
Application filed by Udylite Corp filed Critical Udylite Corp
Priority to US22489A priority Critical patent/US2523191A/en
Application granted granted Critical
Publication of US2523191A publication Critical patent/US2523191A/en
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

  • This invention relates to the electrodeposition of nickel from aqueous acidic nickel baths.
  • the object of this invention is to decrease the grain size and increase the luster and brightness of the nickel deposit without decreasing appreciably the ductility of the plate or the current density range of the nickel bath.
  • Table I are listed a number of alpha and beta. unsaturated alifatic sulfonic acids and their optimum concentrations in the nickel baths. Actually they all can be used up to saturation in the baths, that is, they do not have critical upper concentration limits.
  • the brightness listed in Table I can be used in any type of operating acidic nickel baths with beneficial eil'ects.
  • Table II are listed by way of illustration a number of such acidic nickel baths.
  • the nickel plate obtained with the alpha and beta unsaturated sulfonic acids present in the acidic baths is very fine-grained, of good color and ductile, and remarkably free from pitting. On buifed surfaces the plate obtained is as good in reflectivity and brightness as the base.
  • nickel brightners such as, for example,
  • the bath can tolerate larger concentrations of the zinc cadmium than the plain bath without getting brittle, darkish, poorly adherent plate. This is also true with respect to thallous and mercuric salts in about the same concentrations. It is also true with respect to the impurity, copper, which does not produce any appreciable brightness when present in small concentrations, but tends, instead to very readily produce dark deposits, first appearing at the lowest current densities and extending upward as the concentration of copper is increased.
  • the vinyl and allyl sulfonic acids are extremely good. That is, they are very eiiective for the very low current density values while at the same time being very eifective for the middle and high current density values.
  • beta unsaturated alifatic sulfonic acids (1. e., allyl sulfonic acid) are similar in their eflects in the nickel baths to the alpha unsaturated sulfonic acids (e. g., vinyl sulfonic acid), they diflfer to a certain degree.
  • the vinyl sulfonic acid for example, makes possible a toleration of larger concentrations of materials (both inorganic and organic) which plate out preferentially to nickel and which when alone in the bath cause brittle and easily stained plate or poor color.
  • the beta olefinic double bond as present in allyl sulfonic acid does exert an epect on, or transmits an effect to, the sulfonic group and increases its reactivity, but not as strongly as does an alpha unsaturated bond.
  • the sulfonic group affects the active unsaturation characteristics of the alpha carbon doublebonds more. strongly than the more distant beta, that is, the beta double bonds are more strongly olefinic in character, and thus allyl sulfonic acid also exerts a brightening eflect in a somewhat similar manner as does allyl alcohol, allyl amine, allyl urea, allyl arsenic acid, and acrylic acid.
  • the latter do not increase the toleration of impurities, in fact, they decrease the tolerance.
  • the high nickel chloride bath e. g.,
  • saturated alifatic sulfonic acids when pure, unlike the alpha or beta unsaturated alifatic sulfonic acids, 'do not produce brightness or such desirable effects as an increase in tolerance to materials -which plate out preferentially to nickel and cause deposits of poor color in the low current density areas.
  • Often impure saturated alifatic sulfonic acids tend to produce some transient brightening effects. and this I have found to be due to traces of mercaptans or sulfltes left over from some of the starting materials used in the synthesis.
  • pure ethane sulfonic acid or pure 2-bromo ethane sulfonic acid donot produce any appreciable brightening effect, nor do pure saturated alifatic sulfones such as fSulfonaL"
  • the alpha and beta unsaturated sulfonic acids can be used with beneficial effects in other acidic nickel baths, besides those listed in Table II, for
  • boric acid As far as the cathode film is concerned is boric acid andis preferred, though other buffers can be used, as, for example, formic, citric, or fluoboric acids.
  • Mixtures of compounds of Table I can be used 4 with beneficial eflects (improved brightness of plate) as, for example, ally] sulfonic acid with vinyl sulfonic.
  • beneficial eflects improved brightness of plate
  • mixtures of the compounds of Table I with aryl sulfonates, aryl sulfonamides, aryl sulflmides, aryi sulfone sulfonic acids enhance or improve the brightness ofthe plate.
  • 0.1-.2 g./l. of o-benzoyl sulflmide with 0.1-3 g./1. of vinyl and allyl sulfonic acids In general the nickel salts of the alpha or beta 1 unsaturated alifatic sulfonic acids are preferred for additions instead of the free acids in order not to alter the pH of the baths very much.
  • concentrations as low as 0.1 g./l. of compounds of Table I show beneficial effects over 15 small ranges of current density, though in general at least 1 g./l. concentrations should be used.
  • the alpha andbeta unsaturated sulfonic acids such as the vinyl (ethylene) sulfonic acids and the allyl sulfonic acids are very beneficial when added to acidic nickel baths containing from 7.1 g./l, to saturation .of any one or more of the following: the naphthalenesulfonic acids, the benzene sulfonic acids, the benzene sulfonamides, the diphenyl sulfone sulfonic acids, in that the 25 ductility of the plate and the brightness in the recesses (low current density areas) is improved. This is especially true if the chloride concentration ofsuch nickel baths is above '75 g./l.
  • the allyl sulfonate suppresses hydrogen evolugo a concentration in the bath falling within a range tion and for this reason tends to prevent pitting.
  • nickel baths that employ naphthalene sulfonic acids or benzene sulfonamides or sulfonimides with wetting agents, it is of rather common occurrence that concentrated pitting will start on the underside of work when the baths are contaminated with small amounts of oily material. If to such baths is added about 1 gram per liter of sodium or nickel allyl sulfonate, the rease pitting" or foam pitting is usually eliminated because of the suppression of hydrogen evolution.
  • a bath for electrodepositing fine-grained, lustrous nickel consisting essentially of an aqueous acid solution of a material selected from the group consisting of nickel chloride, nickel sulfate, a mixture of nickel sulfate and nickel chloride, a mixture of nickel fluorborate and nickel chloride, a mixture of nickel fluoborate and nickel sulfate, a mixture of nickel sulfate, nickel chloride and nickel fluoborate, said solution also having dissolved therein an unsaturated organic compound selected from the group consisting of allyl sulfonic acid chlor allyl sulfonic acid and brom allyl sulfonic acid, said unsaturated organic compound having of from about 1 gram per liter to saturation.
  • an unsaturated organic compound selected from the group consisting of allyl sul

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)

Description

Patented Sept. 19, 1950 ELECTRODEPOSITION OF NICKEL FROM AN ACID BATH Henry Brown, Detroit, Mich., assignor to The Udylite Corporation Detroit, Mich., a corporation of Delaware Q No Drawing. Application April 21, 1948, Serial No. 22,489
2, Claims. (Cl. 20449) This invention relates to the electrodeposition of nickel from aqueous acidic nickel baths.
The object of this invention is to decrease the grain size and increase the luster and brightness of the nickel deposit without decreasing appreciably the ductility of the plate or the current density range of the nickel bath.
This object can be accomplished by the addition of certain unsaturated alifatic sulfonic acids such as the alpha and/or beta unsaturated allfatic acids as exemplified by vinyl sulfonic acid (CH2=CHSO3H) and allyl sulfonic acid (CH2=CHCH2SO3H). In Table I are listed a number of alpha and beta. unsaturated alifatic sulfonic acids and their optimum concentrations in the nickel baths. Actually they all can be used up to saturation in the baths, that is, they do not have critical upper concentration limits.
The brightness listed in Table I can be used in any type of operating acidic nickel baths with beneficial eil'ects. In Table II are listed by way of illustration a number of such acidic nickel baths.
The nickel plate obtained with the alpha and beta unsaturated sulfonic acids present in the acidic baths is very fine-grained, of good color and ductile, and remarkably free from pitting. On buifed surfaces the plate obtained is as good in reflectivity and brightness as the base.
It is a surprising and remarkable fact, for example, that in a warm nickel chloride bath (Bath No. 2 300 g./l.NiCl-.-.6H:O and which gives very brittle darkish plate (evidently due to basic salt inclusions) at pH values oi'g4-5, the addition of about 8 g./l. of vinyl sulfonic or allyl sulfonic acid (added as the Ni salt) will produce very ductile fine-grained plate of good luster or brightness and color under otherwise the same conditions, i. e., temperatures, pH values, and current densities whereas 1,5 naphthalene disulfonic acid will not accomplish this, and the plate is still very brittle and of poor color (it is, however, finer grained than the plain nickel chloride bath). These facts also hold true in other high speed plating baths containing high nickel chloride concentrations, for example, 150 g./l. of nickel sulfate and 150 g./l. of nickel chloride. It is also interesting to note that formaldehyde alone at about 1 g./l. also gives brittle, darkish, fine-grained, frosty plate in the high nickel chloride baths.
If other nickel brightners such as, for example,
zinc or cadmium in a concentration of about .brighter than with either material alone in the bath. Also, the bath can tolerate larger concentrations of the zinc cadmium than the plain bath without getting brittle, darkish, poorly adherent plate. This is also true with respect to thallous and mercuric salts in about the same concentrations. It is also true with respect to the impurity, copper, which does not produce any appreciable brightness when present in small concentrations, but tends, instead to very readily produce dark deposits, first appearing at the lowest current densities and extending upward as the concentration of copper is increased. In fact with respect to increasing the tolerance of the nickel bath to such materials which plate out preferentially to the nickel and tend at the slightest excess to discolor the very low current areas, the vinyl and allyl sulfonic acids are extremely good. That is, they are very eiiective for the very low current density values while at the same time being very eifective for the middle and high current density values.
While the beta unsaturated alifatic sulfonic acids (1. e., allyl sulfonic acid) are similar in their eflects in the nickel baths to the alpha unsaturated sulfonic acids (e. g., vinyl sulfonic acid), they diflfer to a certain degree. The vinyl sulfonic acid, for example, makes possible a toleration of larger concentrations of materials (both inorganic and organic) which plate out preferentially to nickel and which when alone in the bath cause brittle and easily stained plate or poor color. Apparently, the beta olefinic double bond as present in allyl sulfonic acid does exert an epect on, or transmits an effect to, the sulfonic group and increases its reactivity, but not as strongly as does an alpha unsaturated bond. Apparently, conversely the sulfonic group affects the active unsaturation characteristics of the alpha carbon doublebonds more. strongly than the more distant beta, that is, the beta double bonds are more strongly olefinic in character, and thus allyl sulfonic acid also exerts a brightening eflect in a somewhat similar manner as does allyl alcohol, allyl amine, allyl urea, allyl arsenic acid, and acrylic acid. The latter, however, do not increase the toleration of impurities, in fact, they decrease the tolerance. For example, in the high nickel chloride bath (e. g.,
vBath No. 2), the addition of sodium or nickel acrylate from 1 g./l. to saturation only produces inner grain but the plate is still dark and very brittle.
It is also interesting to note that saturated alifatic sulfonic acids (when pure), unlike the alpha or beta unsaturated alifatic sulfonic acids, 'do not produce brightness or such desirable effects as an increase in tolerance to materials -which plate out preferentially to nickel and cause deposits of poor color in the low current density areas. Often impure saturated alifatic sulfonic acids tend to produce some transient brightening effects. and this I have found to be due to traces of mercaptans or sulfltes left over from some of the starting materials used in the synthesis. For example, pure ethane sulfonic acid or pure 2-bromo ethane sulfonic acid donot produce any appreciable brightening effect, nor do pure saturated alifatic sulfones such as fSulfonaL" The alpha and beta unsaturated sulfonic acids can be used with beneficial effects in other acidic nickel baths, besides those listed in Table II, for
example, in baths made up with nickel sulfa-.
mate in whole or in part.
The best buffer as far as the cathode film is concerned is boric acid andis preferred, though other buffers can be used, as, for example, formic, citric, or fluoboric acids.
Mixtures of compounds of Table I can be used 4 with beneficial eflects (improved brightness of plate) as, for example, ally] sulfonic acid with vinyl sulfonic. Also mixtures of the compounds of Table I with aryl sulfonates, aryl sulfonamides, aryl sulflmides, aryi sulfone sulfonic acids enhance or improve the brightness ofthe plate. For example, 0.1-.2 g./l. of o-benzoyl sulflmide with 0.1-3 g./1. of vinyl and allyl sulfonic acids. In general the nickel salts of the alpha or beta 1 unsaturated alifatic sulfonic acids are preferred for additions instead of the free acids in order not to alter the pH of the baths very much.
Even concentrations as low as 0.1 g./l. of compounds of Table I show beneficial effects over 15 small ranges of current density, though in general at least 1 g./l. concentrations should be used. The alpha andbeta unsaturated sulfonic acids such as the vinyl (ethylene) sulfonic acids and the allyl sulfonic acids are very beneficial when added to acidic nickel baths containing from 7.1 g./l, to saturation .of any one or more of the following: the naphthalenesulfonic acids, the benzene sulfonic acids, the benzene sulfonamides, the diphenyl sulfone sulfonic acids, in that the 25 ductility of the plate and the brightness in the recesses (low current density areas) is improved. This is especially true if the chloride concentration ofsuch nickel baths is above '75 g./l.
NiC12.6H2O.
TABLE '1 Alpha and beta unsaturated aliphatic sulfonic acids Opt. Conc. (an) n- 1. cnFJ: so,on (Ni. 00, Na, K, or g salt) 1-8 (vinyl sulfonic acid) c1 2. CH:=(IISO;OH (Ni, 00, Na, K, or M salt) i-s Br 1 3. cnpo so,on in, 00, Na, K, or Mg Sm 1-8 H I 4. met-$ 80, (Ni, 00, Na, K, 0! M salt) 1-8 l (allyl sulionic acid) c1 c1 ls. Capt-e40, (Ni, Co, is, K, or M salt) 1-0 H H V e s. Ciao-$0,011 (Ni,Co,Na, K.orMg salt) 1-8 V B O|H CH=CH.CH,SO:OH (Ni, 00, Na, K, 01' Mg salt) 1-8 (2 ohloro allyl sulionate) IIIHH All H (3-chl0ro ally] sulionate) (a-bromo allyl sulfonic acid) TABLE II Butler Other Salts N150; NiCh C urrent 111,0, 011,0, 313 pH Debsity Formula g./l. Formula g./l. amps'lsq' 45 HIBOI (1)0110 acid) 40 75-160 2-6 10-75 300 H1B01 35 75-160 1-5 10-100 225 do 35 75-160 2-6 10-85 45 11C OH(formic acid) 35 75440 3-6 -60 HsBO: 40 45 a? 4 8 75-140 2-6 10-50 F 2 to 4 45 Citric acid (nickel salt) 30 75-140 3 6 10-60 45 B1B a 40 MgSO|.7H 125 75-160 2-0 10-60 3 75 g }Nac1.-.. 4o 75 5.5 10-25 NH Cl 16 9 75 15 75 75 5.3 10-25 10 10o do 15 N 40! 75 5.3 5-20 The allyl sulfonate suppresses hydrogen evolugo a concentration in the bath falling within a range tion and for this reason tends to prevent pitting. In nickel baths that employ naphthalene sulfonic acids or benzene sulfonamides or sulfonimides with wetting agents, it is of rather common occurrence that concentrated pitting will start on the underside of work when the baths are contaminated with small amounts of oily material. If to such baths is added about 1 gram per liter of sodium or nickel allyl sulfonate, the rease pitting" or foam pitting is usually eliminated because of the suppression of hydrogen evolution.
This application is a continuation-in-part of my copendi'ng application Serial No. 603,753,
filed July 7, 1945.
Iclaim:
1. A bath for electrodepositing fine-grained, lustrous nickel consisting essentially of an aqueous acid solution of a material selected from the group consisting of nickel chloride, nickel sulfate, a mixture of nickel sulfate and nickel chloride, a mixture of nickel fluorborate and nickel chloride, a mixture of nickel fluoborate and nickel sulfate, a mixture of nickel sulfate, nickel chloride and nickel fluoborate, said solution also having dissolved therein an unsaturated organic compound selected from the group consisting of allyl sulfonic acid chlor allyl sulfonic acid and brom allyl sulfonic acid, said unsaturated organic compound having of from about 1 gram per liter to saturation.
2. A method for electrodepositing fine-grained, lustrous nickel comprising the step of electrodepositing fine-grained, lustrous nickel from an aqueous acid solution consisting essentially of a material selected from the group consisting of nickel chloride, nickel sulfate, a mixture of nickel sulfate and nickel chloride, a mixture of nickel 'fiuoborate and nickel chloride, a mixture of nickel fiuoborate and nickel sulfate, a mixture of nickel sulfate, nickel chloride and nickel fluoborate, said solution also having dissolved therein an unsaturated organic compound selected from the group consisting of allyl sulfonic acid (CH2=CHCH2SO3H), chlor allyl sulfonic acid and brom allyl sulfonic acid, said unsaturated organic compound having a concentration in the bath falling within a range 01' from about 1 gram per liter to saturation.
HENRY BROWN.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number

Claims (1)

1. A BATH FOR ELECTRODEPOSITING FINE-GRAINED, LUSTROUS NICKEL CONSISTING ESSENTIALLY OF AN AQUEOUS ACID SOLUTION OF A MATERIAL SELECTED FROM THE GROUP CONSISTING OF NICKEL CHLORIDE, NICKEL SULFATE, A MIXTURE OF NICKEL SULFATE AND NICKEL CHLORIDE, A MIXTURE OF NICKEL FLUORBORATE AND NICKEL CHLORIDE, A MIXTURE OF NICKEL FLUOBORATE AND NICKEL SULFATE, A MIXTURE OF NICKEL SULFATE, NICKEL CHLORIDE AND NICKEL FLUOBORATE, SAID SOLUTION ALSO HAVING DISSOLVED THEREIN AN UNSATURATED ORGANIC COMPOUND SELECTED FROM THE GROUP CONSISTING OF ALLYL SULFONIC ACID
US22489A 1945-07-07 1948-04-21 Electrodeposition of nickel from an acid bath Expired - Lifetime US2523191A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US22489A US2523191A (en) 1945-07-07 1948-04-21 Electrodeposition of nickel from an acid bath

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US603753A US2523190A (en) 1945-07-07 1945-07-07 Electrodeposition of nickel from an acid bath
US22489A US2523191A (en) 1945-07-07 1948-04-21 Electrodeposition of nickel from an acid bath

Publications (1)

Publication Number Publication Date
US2523191A true US2523191A (en) 1950-09-19

Family

ID=26695982

Family Applications (1)

Application Number Title Priority Date Filing Date
US22489A Expired - Lifetime US2523191A (en) 1945-07-07 1948-04-21 Electrodeposition of nickel from an acid bath

Country Status (1)

Country Link
US (1) US2523191A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2550449A (en) * 1946-04-20 1951-04-24 Udylite Corp Electrodeposition of nickel from an acid bath
DE1001078B (en) * 1953-08-13 1957-01-17 Dehydag Gmbh Galvanic baths for the production of metal coatings
US3515564A (en) * 1968-05-27 1970-06-02 Allied Res Prod Inc Stabilization of electroless plating solutions
US6045682A (en) * 1998-03-24 2000-04-04 Enthone-Omi, Inc. Ductility agents for nickel-tungsten alloys

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1818229A (en) * 1928-02-23 1931-08-11 Grasselli Chemical Co Electroplating
US2029387A (en) * 1934-03-14 1936-02-04 Harshaw Chem Corp Method and means of electrodeposition
US2112818A (en) * 1934-08-15 1938-03-29 Mcgean Chem Co Inc Electrodeposition of metals
US2125229A (en) * 1936-04-14 1938-07-26 Harshaw Chem Corp Electrodeposition of metals
US2171842A (en) * 1936-07-13 1939-09-05 Du Pont Electroplating
US2198267A (en) * 1939-12-14 1940-04-23 Harshaw Chem Corp Electrodeposition of metals

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1818229A (en) * 1928-02-23 1931-08-11 Grasselli Chemical Co Electroplating
US2029387A (en) * 1934-03-14 1936-02-04 Harshaw Chem Corp Method and means of electrodeposition
US2112818A (en) * 1934-08-15 1938-03-29 Mcgean Chem Co Inc Electrodeposition of metals
US2125229A (en) * 1936-04-14 1938-07-26 Harshaw Chem Corp Electrodeposition of metals
US2171842A (en) * 1936-07-13 1939-09-05 Du Pont Electroplating
US2198267A (en) * 1939-12-14 1940-04-23 Harshaw Chem Corp Electrodeposition of metals

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2550449A (en) * 1946-04-20 1951-04-24 Udylite Corp Electrodeposition of nickel from an acid bath
DE1001078B (en) * 1953-08-13 1957-01-17 Dehydag Gmbh Galvanic baths for the production of metal coatings
US3515564A (en) * 1968-05-27 1970-06-02 Allied Res Prod Inc Stabilization of electroless plating solutions
US6045682A (en) * 1998-03-24 2000-04-04 Enthone-Omi, Inc. Ductility agents for nickel-tungsten alloys

Similar Documents

Publication Publication Date Title
US2830014A (en) Electroplating process
US2849351A (en) Electroplating process
GB808104A (en) Electrodeposition of copper from aqueous alkaline cyanide solutions
US2523190A (en) Electrodeposition of nickel from an acid bath
US2318592A (en) Electrodeposition
US2147415A (en) Electroplating
US2523191A (en) Electrodeposition of nickel from an acid bath
US2882208A (en) Electrodeposition of nickel
US2466677A (en) Electrodeposition of nickel from an acid bath
US2550449A (en) Electrodeposition of nickel from an acid bath
US2849353A (en) Bright nickel plating
US2389179A (en) Electrodeposition of metals
US3220940A (en) Electrodeposition of nickel
US2427280A (en) Nickel electroplating composition
US2181773A (en) Brass plating
US2654703A (en) Electrodeposition of bright nickel, cobalt, and alloys thereof
US2972571A (en) Nickel plating solutions
US2986500A (en) Electrodeposition of bright nickel
GB1234793A (en) Brightening and hardening additive for electrolytic silvering baths
US2455555A (en) Electrodeposition of nickel from an acid bath
US2539588A (en) Electrodeposition of nickel
US2648628A (en) Electroplating of nickel
US3219558A (en) Bright silver plating bath and process
US2402801A (en) Electrodeposition of nickel
US3898138A (en) Method and bath for the electrodeposition of nickel