US3285840A - Process and composition for zinc electrodeposition - Google Patents

Process and composition for zinc electrodeposition Download PDF

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Publication number
US3285840A
US3285840A US282138A US28213863A US3285840A US 3285840 A US3285840 A US 3285840A US 282138 A US282138 A US 282138A US 28213863 A US28213863 A US 28213863A US 3285840 A US3285840 A US 3285840A
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Prior art keywords
aldehyde
zinc
meat
agent
enzyme
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Expired - Lifetime
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US282138A
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English (en)
Inventor
Karl H Lindemann
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MacDermid Enthone Inc
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Enthone Inc
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Filing date
Publication date
Priority to GB1051624D priority Critical patent/GB1051624A/en
Application filed by Enthone Inc filed Critical Enthone Inc
Priority to US282138A priority patent/US3285840A/en
Priority to FR975196A priority patent/FR1403916A/fr
Priority to DEJ25873A priority patent/DE1266097B/de
Application granted granted Critical
Publication of US3285840A publication Critical patent/US3285840A/en
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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
    • C25D3/22Electroplating: Baths therefor from solutions of zinc

Definitions

  • the present invention is of the nature of a discovery. It stems out of the finding that hydrolyzed meat of animal origin, particularly a protein hydrolysate of the kind produced by the action of a proteolytic enzyme, can be used to excellent advantage as a brightener. Not only does hydrolyzed meat, so used, tend to produce a brighter deposit directly from the plating bath, but for reasons not understood its use makes it possible to employ in plating baths of the acid-zinc type brighteners of kinds that in the past have been found to be useful only in cyanide-zinc plating.
  • aldehyde brighteners of kinds heretofore employed in cyanide-zinc plating impart greater brightness, give improved leveling, and yield a more refined crystal structure when used in conjunction with hydrolyzed meat in an acid-zinc plating bath.
  • Their use also serves to enlarge the eifective range of the plating bath both in respect of the temperature and in respect of the hydrogen ion concentration (pl-I).
  • a typical acid-zinc plating bath of a kind that may be used in the present invention contains water as a solvent or continuous phase, Zinc sulph-ate (ZnSO -7-H O) in an amount between about 40 and about 46 ounces per gallon, an inorganic acid such as boric acid (H BO in an amount in the neighborhood of 4 ounces per gallon, and often a conductive salt such as ammonium chloride (NH CI) or ammonium fluoride (NH F), likewise in an amount in the neighborhood of 4 ounces per gallon.
  • Zinc chloride, zinc acetate and aluminum sulphate (Al (SO '18H O) are sometimes used in amounts of the order or about 2 to 4 ounces per gallon. If the addition agent of the present invention is added as below described, such a bath can be used over a temperature range which may go as low as 80 and as high as 130 F. In a typical case, its hydrogen ion concentration (pH) will between 3 and 4.
  • a conventional anti-pitting agent such as the sodium salt of dodecylated oxydibenzene disulphonate.
  • this compound operates as an anionic surfactant or surface active agent. It is available in the form of a 45% solution under the trademark Benax 2A1. While it may be omitted entirely if desired, in the normal practice of the invention it is incorporated in the plating bath by adding to each 1000 gallons from 4 to 8 gallons of the solution obtained by diluting 20 gallons of the commercial product with 180 gallons of water.
  • the novel addition agent that is one of the features of the present in vention.
  • it comprises water, a s face-active agent of the nature of a wetting agent, and, present in a discrete or discontinuous phase, degraded meat of animal origin, more particularly the protein hydrolysate obtained therefrom by subjecting to the meat the action of a pancreatic or similar proteolytic enzyme.
  • Enzyme-degraded meats certain of which are used as bacteriological nutrients, are readily available on the commercial market.
  • a shipped, degrated meat of this kind takes the form of a dry powder containing up to about 5% of water.
  • Approximately 95% of the commercial product consists largely of not entirely of hydrolyzed meat protein, fatty acids and hydrocarbons. Fatty acids, hydrocarbons and the like can total as much as 30% of the commercial product.
  • the remainder, approximately of the commercial product, is proteinaceous material that is virtually completely hydrolyzed.
  • the commercial product contains about 14% total nitrogen, of which about one fifth is believed to be animo nitrogen.
  • the hydrolyzed meat is known to be present in colloidal form in the addition agent, it can probably be accurately described as a protective colloid.
  • the solubilized aldehyde or aldehydes may be any of a rather large class of aldehydes some of the members of which have in common the fact, inter alia, that they have been used successfully in the past in cyanide-zinc plating. In general, the most important of the latter group are anisic aldehyde, veratraldehyde, piperonal and vanillin.
  • aldehyde or aldehydes need not and in certain cases cannot be solubilized by reactions and techniques analogous to those heretofore employed in cyanide-zinc plating but should in each case be solubilized by reaction with an alkali metal bisulphite or some functionally equivalent solubilizer that is compatible with a plating bath of the acid-zinc type.
  • Sodium bisulphite if used as a solubilizer, should be used in quantities that are equimolal in relation to the aldehydes. An excess of an alkali metal bisulphite, if present, is objectionable for the reason that it tends to discolor the deposited zinc. An excess of aldehyde is of no value.
  • the addition agent of the present invention also contains a surface-active agent of the nature of a wetting agent.
  • a surface-active agent of the nature of a wetting agent.
  • the best of the presently available surface-active agents is thought to. be an alkali metal salt of a sulphate of a long chain aliphatic hydrocarbon.
  • a good example is sodium tetradecyl sulphate, an anionic surface-active agent that is available under the trademark Tergitol 4. It is supplied in the form of an aqueous solution of 26 to 28% concentration. It is recognized as a wetting agent 3 lending itself to use in solutions containing relatively low concentrations of dissolved solids. In place of it may be used the sodium salt of 2-ethylhexyl sulphate.
  • This product which likewise is anionic, is sold under the trademark Tergitol 8.
  • the addition agent of the present invention prefer-ably will contain a suitable commercial preservative.
  • a suitable commercial preservative By incorporating such a preservative, the pot life of the addition agent may be extended from a few weeks to more than a year.
  • the preferred preservative is Dowicide B, which is the sodium salt of 2,4,5-trichlorophenol.
  • the addition agent of the invention normally contains the following:
  • 100 gallons can be made up by adding to sufficient water approximately 40 lbs. of enzyme-degraded meat, 8 lbs. of wetting agent solution, 16 lbs. of aldehyde, 12% lbs. of anhydrous sodium bisulphite and 5 oz. of preservative. Most of the foregoing weights are on a non-dry or gross basis.
  • An acceptable procedure calls for dissolving the enzyme-degraded meat in 60 gallons of water at 160 F. in a stainless steel vessel, adding sulphuric acid to lower the pH to 3.5, mixing for about one hour and adding the Tergitol 4 and Dowicide B and mixing for a further period of thirty minutes.
  • the aldehyde and sodium bisulphite should be added, after which the solution should be mixed for thirty minutes. It should then be added to the original mixture in the previously mentioned stainless steel tank. The resulting mixture should be maintained at a temperature of between 140 and 150 F. for an hour, mixed in the meanwhile and then filtered through a suitable filter such as the Udylite filter.
  • the addition of the aldehyde and the solubilizer for the aldehyde can best follow the addition of the meat. It may precede or follow the addition of the Wetting agent. Assuming that the meat has already been added, the introduction of the aldehyde and the solubilizer for the aldehyde immediately produces a heavy precipitate that consists mainly of the fatty acids and hydrocarbons introduced as part of the meat. It is important that the precipitated fatty acids and hydrocarbons should be filtered off. If they are permitted to remain, they tend to produce pitting or at least to interfere with the action of the anti-pitting agent in the plating bath.
  • Example III Meat protein hydrolysate 5 Tergitol 04 1 Heliotropin aldehyde 2 Sodium bisulphite 1.5 Water, q.s.
  • Example IV Meat protein hydrolysate 5 Tergitol 04 1 Veratr-aldehyde 2 Sodium bisulphite 1.5 Water, q.s.
  • Example V Meat protein hydrolysate 5 Tergitol 04 1 2-methy1 2-ethyl 3-hydroxy propionaldehyde 2 Sodium bisulphite 1.5 Water, q.s.
  • Example VI Meat protein hydrolysate 5 Tergitol 04 1 2,4-dichlorobenzaldehyde 2 Sodium bisulphite 1.5 Water, q.s.
  • the preferred procedure is to add to 1000 gallons thereof equal volumes of the addition agent of the present invention and the previously described 5% solution of the anti-pitting agent.
  • the two may be added in amounts of from 4 to 8 gallons, the smaller quantity being for use at the lower end of the temperature range F.) and the greater for use at the upper end of the temperature range F.).
  • the improvement which comprises having present in said electrolyte as brightener an effective amount of an enzyme-degraded hydrolyzed meat protein and of an aldehyde selected from the group consisting of veratraldehyde, anisic aldehyde, piperonal, vanillin, 2,4-dichlorobenzaldehyde, and Z-methyl Z-ethyl 3-hydroxy propionaldehyde.
  • hydrolyzed meat in the form in which it is used in the process consists essentially of an enzyme-degraded meat protein hydrolysate that is substantially free of fatty acids.
  • hydrolysate is derived from meat that has been subjected to a degrading action induced by a proteolytic enzyme.
  • a process according to claim 1 further characterized in that an alkali metal bisulphite is present in the electrolyte in amount suflicieut to solubilize the aldeyhyde.
  • an aqueous acid-zinc electroplating bath comprising, having present in said bath an eifective amount, sufficient to impart brightness to the zinc electroplate, of an enzyme-degraded hydrolyzed meat protein and of an aldehyde selected from the group consisting of veratraldehyde, anisic, aldehyde, piperonal, vanillin, 2,4-dichlorobenzaldehyde and 2-methyl 1 .-ethyl 3- hydroxy propionaldehyde.
  • a plating bath according to claim 6 wherein the hydrolyzed meat consists essentially of a meat protein hydrolysate that is substantially free of fatty acids.
  • hydrolysate is derived from meat that has. been subjected to a degrading action induced by a proteolytic enzyme.
  • a plating bath according to claim 6 further characterized in that an alkali metal bisulphite is present in the bath in amount suflicient to solubilize the aldehyde.
  • a plating bath according to claim 6 further characterized in containing a wetting agent.
  • a plating bath according to claim 10 further characterized in containing an anionic surface active anti-pitting agent.
  • An addition agent for a plating bath consisting essentially of water, an aldehyde selected from the group consisting of veratraldehyde, anisic aldehyde, piperonal, vanillin, 2,4-dichlorobenzaldehyde and Z-methyl 2-ethy1 3- hydroxy propionaldehyde, and an enzyme-degraded hydrolyzed meat protein.
  • hydrolyzed meat protein consists essentially of an enzyme-degraded meat protein hydrolysate that is substantially free of fatty acids.
  • hydrolysate is derived from meat that has been subjected to a degrading action induced by a proteolytic enzyme.
  • An addition agent for a plating bath consisting essentially of water, a wetting agent, an aldehyde selected from the group consisting of veratraldehyde, anisic aldehyde, piperonal, vanillin, hyroxybenzaldehyde, 2,4-dichlorobenzaldehyde and 2-methyl 2-ethyl 3-hydroxy propionaldehyde, and an enzyme-degraded hydrolyzed meat protein.
  • hydrolyzed meat consists essentially of a meat protein hydrolysate that is substantially free of fatty acids.
  • An addition agent for a plating bath consisting essentially of 2.5% to 7.5% of an enzyme-degraded hydrolyzed meat protein, 1% to 5% of an aldehyde selected from the group consisting of veratraldehyde, anisic aldehyde, piperonal, vanillin, 2,4-dichlorobenzaldehyde and 2-methyl 2-ethyl 3-hydroxy propionaldehyde, 0.5% to 1.5% of a wetting agent, 1% to 5% of an alkali metal bisulfite, and 81% to of water, the percentage being by weight.
  • An aqueous electroplating bath for acid zinc plating consisting essentially of between about 40 and about 46 ounces per gallon of zinc sulphate, about 4 ounces per gallon of boric acid, and about 4 ouncesv per gallon of ammonium chloride, and having added thereto per 1,000 gallons thereof, from 4 to 8 gallons of the addition agent of claim 19 and from 4 to 8 gallons of a 5% aqueous solution of an anionic surface active anti-pitting agent, the additive agent and the anti-pitting agent aqueous solution being added in equal volume to the acid zinc bath.
  • An addition agent for a plating bath consisting essentially of an enzyme-degraded hydrolyzed meat protein and an aldehyde selected from the group consisting of veratraldehyde, anisic aldehyde, piperonal, vanillin, 2,4- dichlorobenzaldehyde and Z-methyl 2-ethyl 3-hydroxy propionaldehyde.

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  • 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)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Meat, Egg Or Seafood Products (AREA)
US282138A 1963-05-21 1963-05-21 Process and composition for zinc electrodeposition Expired - Lifetime US3285840A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
GB1051624D GB1051624A (pt) 1963-05-21
US282138A US3285840A (en) 1963-05-21 1963-05-21 Process and composition for zinc electrodeposition
FR975196A FR1403916A (fr) 1963-05-21 1964-05-20 Bain pour le dépôt électrolytique du zinc et agent d'addition destiné à ce bain
DEJ25873A DE1266097B (de) 1963-05-21 1964-05-21 Saures galvanisches Zinkbad und Zusatzmittel fuer dasselbe

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US282138A US3285840A (en) 1963-05-21 1963-05-21 Process and composition for zinc electrodeposition

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850766A (en) * 1974-03-28 1974-11-26 Sterwin Chem Inc Electroplating brightener compositions and process
US20050277074A1 (en) * 2004-06-10 2005-12-15 Zinn Ben T Stagnation point reverse flow combustor
US20060029894A1 (en) * 2004-06-10 2006-02-09 Zinn Ben T Stagnation point reverse flow combustor for a combustion system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA580302A (en) * 1959-07-28 J. Jendrzynski Hillard Method for plating metal using histones and protamines as bath additives
US2898449A (en) * 1956-12-08 1959-08-04 Vreugdenhil Adrianus Signal lamp
US3088884A (en) * 1960-11-07 1963-05-07 Metal & Thermit Corp Electrodeposition

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE714829C (de) * 1939-07-03 1941-12-08 Rasselsteiner Eisenwerksgesell Verfahren zur elektrolytischen Abscheidung glaenzender Zinkniederschlaege auf anderen Metallen

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA580302A (en) * 1959-07-28 J. Jendrzynski Hillard Method for plating metal using histones and protamines as bath additives
US2898449A (en) * 1956-12-08 1959-08-04 Vreugdenhil Adrianus Signal lamp
US3088884A (en) * 1960-11-07 1963-05-07 Metal & Thermit Corp Electrodeposition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850766A (en) * 1974-03-28 1974-11-26 Sterwin Chem Inc Electroplating brightener compositions and process
US20050277074A1 (en) * 2004-06-10 2005-12-15 Zinn Ben T Stagnation point reverse flow combustor
US20060029894A1 (en) * 2004-06-10 2006-02-09 Zinn Ben T Stagnation point reverse flow combustor for a combustion system
US7168949B2 (en) 2004-06-10 2007-01-30 Georgia Tech Research Center Stagnation point reverse flow combustor for a combustion system
US7425127B2 (en) 2004-06-10 2008-09-16 Georgia Tech Research Corporation Stagnation point reverse flow combustor

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DE1266097B (de) 1968-04-11
GB1051624A (pt)

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