EP0037634A1 - Bains de zingage et additifs pour ceux-ci - Google Patents

Bains de zingage et additifs pour ceux-ci Download PDF

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Publication number
EP0037634A1
EP0037634A1 EP19810300833 EP81300833A EP0037634A1 EP 0037634 A1 EP0037634 A1 EP 0037634A1 EP 19810300833 EP19810300833 EP 19810300833 EP 81300833 A EP81300833 A EP 81300833A EP 0037634 A1 EP0037634 A1 EP 0037634A1
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EP
European Patent Office
Prior art keywords
zinc
ring
composition according
per litre
solution
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.)
Withdrawn
Application number
EP19810300833
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German (de)
English (en)
Inventor
Clive Hasdell
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.)
Solvay Solutions UK Ltd
Original Assignee
Albright and Wilson Ltd
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 Albright and Wilson Ltd filed Critical Albright and Wilson Ltd
Publication of EP0037634A1 publication Critical patent/EP0037634A1/fr
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/22—Electroplating: Baths therefor from solutions of zinc

Definitions

  • This invention relates to zinc plating baths and additives therefor and in particular alkaline aqueous plating baths for the electrodeposition of zinc.
  • Many additives have been proposed to improve the deposits from cyanide free alkaline zinc plating baths. Among these additives are aromatic aldehydes and ketones, polyalkylene glycols, polyamines, sulphones and sulphonates, polyphosphates, silicates, Group VI and Group VII metals and reaction products of a compound comprising a heterocyclic ring with at least 2 ring nitrogen atoms, and an epihalogenohydrin (see BP 1553265).
  • Additives (a) and (b) appear to work together in a synergistic fashion since neither additive alone, when added to an alkaline cyanide free zinc plating bath, produces bright zinc deposits over a wide range of current densities.
  • Our invention therefore provides according to a first aspect a brightening composition for a zinc plating bath comprising (a) a betaine containing a quaternary nitrogen atom and a carboxylic or sulphonic acid group and (b) a reaction product of an epihalohydrin and a heterocyclic compound containing a nitrogen ring atom.
  • the betaine is an organic compound which is an internal salt having a zwitterionic, polar character so that it has a cationic group and an anionic group within its molecule.
  • the cationic group is a quaternary nitrogen atom.
  • the anionic group is a carboxylic or sulphonic acid group which is joined to the quaternary nitrogen atom via at least one carbon atom and usually via a chain of up to six carbon atoms.
  • the quaternary nitrogen atom typically forms part of a five-membered or preferably six-membered heterocyclic ring which is usually unsaturated, preferably aromatic and may have two nitrogen ring atoms as in imidazolinium and pyrazinium compounds or preferably one nitrogen ring atom as in pyrrolium and pyridinium compounds, all other atoms in the heterocyclic ring being preferably carbon atoms.
  • the betaine may contain attached to the heterocyclic ring, especially in a fused relationship thereto, a carbocyclic ring, preferably six-membered, especially unsaturated, e.g.
  • an aromatic ring as in a betaine derived from benzimidazole or quinoxaline or more preferably from indole, quinoline or isoquinoline. It is preferred, however, that the betaine contain no ring other than the said heterocyclic ring.
  • One or more carbon ring atoms in the betaine may each be substituted by a group such as: hydroxide; cyanide; amino or amido, optionally substituted by an alkyl group having from one to four carbon atoms; hydrazino or hydrazido; halide, e.g. bromide or chloride; alkyl, alkenyl or alkynyl, each preferably of 1-6 carbon atoms, e.g.
  • betaines are quaternary derivatives of pyridine compounds such as, for example, pyridine, 4-cyanopyridine, picolinic acid, 2-picoline, nicotinamide and butyl nicotinate.
  • the carboxylic or sulphonic acid group may be joined directly to a carbon ring atom either in the said heterocyclic ring or, less preferably, in any carbocyclic ring which may be attached thereto.
  • the acid group may be a substituent in an alkyl group which is joined directly to the quaternary nitrogen atom.
  • betaines which have the acid group joined to the heterocyclic ring at the quaternary nitrogen atom are isoquinoline N-betaine and indole N-propyl sulphobetaine.
  • Preferred pyridinium betaines include propyl nicotinate N-betaine and 4-picoline N-butyl sulphobetaine.
  • a hydrocarbon group generally a monovalent group such as an alkyl, alkenyl or alkynyl group usually having from one to four carbon atoms, e.g. methyl or allyl, an aralkyl group e.g. of 7 to 19 carbon atoms such as benzyl, or less preferably an aryl group e.g. an aromatic hydrocarbyl group of 6 to 18 carbon atoms such as phenyl.
  • the hydrocarbon group may be a divalent group such as an alkylene or aralkylene group e.g.
  • the hydrocarbon group may be unsubstituted or may be substituted by one or more groups such as alkyl or alkoxy having from one to four carbon atoms, phenyl, halogen, hydroxy and cyanide.
  • Examples of monovalent optionally substituted hydrocarbon groups are 4-methyl benzyl, 4-chloro benzyl, allyl and propargyl.
  • the acid group is generally joined to a carbon ring atom and is preferably joined at the 3- or 4- position, more preferably at the 3- position especially where the acid group is the only substituent on any carbon ring atom, particularly in a pyridinium betaine.
  • Pyridinium 4-sulphonates, pyridinium 4-carboxylates, especially pyridinium 3- sulphonates and more especially pyridinium 3- carboxylates are preferred, e.g. N-allyl pyridinium 3-carboxylate, N-ethyl pyridinium 3- carboxylate and N-(4-chloro benzyl) pyridinium 3-carboxylate.
  • the most preferred compounds are N-methyl pyridinium 3-carboxylate and especially N-benzyl pyridinium 3-carboxylate.
  • the epihalohydrin may be epibromhydrin or preferably epichlorhydrin.
  • the heterocyclic compound contains at least one nitrogen ring atom usually in a six-membered or preferably five-membered heterocyclic ring.
  • the ring preferably contains at least two nitrogen ring atoms, usually two or three, especially two.
  • the nitrogen ring atoms may be secondary or tertiary nitrogen atoms but preferably the ring contains at least one secondary nitrogen ring atom. More preferably it also contains at least one tertiary nitrogen ring atom.
  • Aromatic heterocyclic compounds are preferred, which the nitrogen atom or atoms form part of the aromatic ring.
  • the heterocyclic compound preferably consists of one six-membered or especially five-membered ring, optionally substituted by at least one group such as: hydroxide; halide, e.g. chloride; amino; alkoxy, alkanoyl or hydrocarbon such as alkyl, alkenyl or alkynyl usually having from one to four carbon atoms, e.g. ethoxy, acetyl, butyl, allyl.
  • these substituted heterocyclic compounds are: 1,4-diethyl piperazine; 2,5-dimethyl piperazine; 1-acetyl pyrrole; 4-hydroxy, 2-amino imidazole.
  • the heterocyclic compound comprises in addition to one heterocyclic ring, also in a fused or unfused relationship thereto a carbocyclic ring or a second heterocyclic ring, preferably six-membered especially unsaturated, e.g. an aromatic ring containing up to two nitrogen heteroatoms, as in for example, purine, pteridine, benzimidazole and their derivatives.
  • the first or only heterocyclic ring preferably contains only carbon and nitrogen ring atoms but may also contain other ring atoms such as sulphur or oxygen, as in, for example 1,2,3 oxadiazole and benzothiadiazine.
  • suitable heterocyclic compounds are triazines, triazoles, preferably diazines and more preferably diazoles such as imidazole and substituted imidazoles, such as: 1-methyl imidazole; 1-ethyl imidazole; 2-methyl imidazole; 1,4-dimethyl imidazole; 1-ethyl, 2-methyl imidazole; 1-oxymethyl imidazole (hydroxymethyl imidazole); 5-ethyl, 4-hydroxy imidazole; 1-vinyl imidazole.
  • Other useful compounds are piperazine and substituted piperazines, e.g. piperazines with at least one hydrocarbon substituent such as 1,4-dimethyl piperazine.
  • the reaction product may be prepared, for example, by dissolving the heterocyclic compound in a solvent such as water, adding the epihalohydrin in a molar ratio of from 1:0.5 to 1:8, e.g. from 1:1 to 1:4 and allowing them to react at a temperature of from 40 0 C to the boiling point, e.g. from 50 0 C to 90 0 C, such as 70-85 0 C, for e.g. from 1 to 10 hours until reaction is complete.
  • the resulting solution of reaction product may be used as such in compositions of our invention. There is no need to isolate the reaction product (b) from solution before adding the betaine (a) to it.
  • compositions comprising mixtures of (a) and (b) in which the molar ratio of the betaine (a) to the heterocyclic compound used in preparing (b) is from 1:1 to 1:30, preferably from 1:4 to 1:25, such as from 1:6 to 1:20, e.g. from 1:7 to 1:14, are particularly effective as brightening agents for aqueous alkaline zinc plating baths. It is convenient to prepare such compositions as aqueous solutions by mixing an aqueous solution of (a) with an aqueous solution of (b) prepared by the method suggested above.
  • the resulting aqueous composition preferably contains from 0.01 to 1 moles more preferably from 0.02 to 0.5 moles, especially from 0.04 to 0.2 moles of betaine (a) per litre of solution. It generally contains a quantity of reaction product (b) prepared from 0.01 to 10 moles, usually from 0.1 to 4 moles especially from 0.4 to 2 moles of heterocyclic compound per litre of solution.
  • our invention provides an aqueous solution comprising from 0.01 to 1 mole per litre of solution of a betaine containing a quaternary nitrogen atom and a carboxylic or sulphonic acid group and a reaction product of an epihalohydrin with a heterocyclic compound containing a nitrogen ring atom,the quantity of reaction product per litre of solution being derived from 0.01 to 10 moles heterocyclic compound in a ratio of from 1 to 30 moles of heterocyclic compound per mole of betaine.
  • the aqueous solution comprising betaine and reaction product may be used as a brightening agent for an aqueous alkaline zinc plating bath and will generally be added thereto in proportions of from 1 to 100 ml, e.g. from 2 to 25 ml of aqueous solution per litre of zinc plating bath.
  • the aqueous solution preferably contains in addition polyvinyl alcohol in the proportions of from 1 to 100g per litre of aqueous solution.
  • an alkaline aqueous, preferably cyanide-free, zinc plating bath comprising (a) a betaine containing a quaternary nitrogen atom and a carboxylic or sulphonic acid group and (b) a reaction product of an epihalohydrin with a heterocyclic compound containing a nitrogen ring.
  • a bath of our invention will generally be operated under strongly alkaline conditions e.g. at a pH above 12 and preferably above 13. This pH is usually obtained by adding to water an alkali metal hydroxide such as potassium hydroxide or preferably sodium hydroxide in amounts such as to form aqueous solutions containing from 30 to 180g preferably from 60 to 130g of sodium hydroxide per litre of solution.
  • a barrel plating bath usually contains slightly more sodium hydroxide per litre of solution than a rack plating bath.
  • a barrel plating bath may, for example, contain from 90 to 130g e.g. 110g of sodium hydroxide per litre of solution and a rack plating bath may contain from 60 to 100g e.g. 80g of sodium hydroxide per litre of solution.
  • Zinc may be added to the bath in the form of a bath-soluble zinc compound such as zinc oxide or zinc hydroxide or, less preferably, a zinc salt such as zinc sulphate, or zinc metal.
  • the bath will generally contain from 4 to 15g preferably from 6 to 13g of zinc per litre of solution.
  • a barrel plating bath usually contains slightly more zinc per litre of solution than a rack plating bath.
  • a barrel plating bath may, for example, contain from 9 to 13g e.g. llg of zinc per litre of solution and a rack plating bath may contain from 6 to lOg e.g. 8g of zinc per litre of solution.
  • the weight ratio of sodium hydroxide to zinc is usually from about 8:1 to about 12:1, preferably 10:1, in both barrel plating and rack plating baths.
  • the bath may contain from 2x10 -5 to 10 -2 moles preferably from 5 x 10 -5 to 5 x 10 -3 moles especially from 10- 4 to 3 x 10- 3 moles, e.g. from 2 x 10 -4 to 10 -3 moles of betaine (a) per litre of solution.
  • Additive (b) may be present in concentrations per litre of solution prepared from 5 x 10 -4 to 5 x 10 -2 moles preferably from 8x10 -4 to 3 x 10- 2 moles especially from 10 -3 to 2 x 10 -2 moles, e.g. from 2 x 10 -3 to 10- 2 moles of heterocyclic compound.
  • Additives (a) and (b) may be added separately, preferably in aqueous solution or mixed together especially in the form of an aqueous composition according to the second aspect of this invention.
  • An alkaline zinc plating bath may be produced by mixing water, zinc compound, sodium hydroxide and additives (a) and (b).
  • a bath consisting of these components may generally be used to electrodeposit bright, ductile zinc over a wide range of current densities, up to 100 amperes per square foot (ASF) (11A dm -2 ), or even 150 ASF (17A dm -2 ). It is particularly useful over the range from 0.1 to 100 ASF (from 0.011 to 11A dm -2 ) and especially advantageous from 60 to 100 ASF (from 6.5 to 11 dm- 2 ). This extension of the bright plating range to current densities above 60 A S F (6.5A dm- 2 ) means that bright plated articles can be .
  • polyalkylene polyamines especially those of formula H 2 N-C(CH 2 ) n NH] x H where n is from 2 to 4 and x is from 8 to 150 are preferably substantially absent.
  • the bath usually contains from 0.005 to 10 gram per litre of solution of polyvinyl alcohol to reduce the haziness of the bright zinc deposit.
  • Complexants such as gluconate and ethylene diamine tetraacetic acid may optionally be present in concentrations of up to 1 gram of complexant per litre of solution.
  • a typical plating bath may be prepared by dissolving sodium hydroxide in water adding zinc oxide and diluting the solution to working concentrations with more water.
  • Generally heavy metal contaminants will be removed from the bath before use by a conventional method e.g. by using the bath to electrodeposit at less than 10 ASF (l.lA dm- 2 ) for at least one ampere hour per litre of solution.
  • An aqueous mixture of additives (a) and (b) in suitable proportions and generally mixed with polyvinyl alcohol may then be added and the bath may be used to electrodeposit bright, ductile zinc over a wide range of current densities.
  • the plating baths are used to plate articles having metal surfaces e.g. ferrous metal surfaces such as iron or steel or nonferrous metal surfaces such as zinc or brass surfaces.
  • An aqueous solution of a reaction product (R) was prepared by mixing imidazole (0.18 moles) with water (70g) adding epichlorhydrin (0.33) moles and refluxing at 80°C for 4 hours.
  • a steel component was thoroughtly cleaned in an alkaline soap cleaner, rinsed, and etched in 50% v/v hydrochloric acid, rinsed and immersed in a zinc plating bath made up as in Example 1 for twenty minutes at an average current density of 20 ASF at 20 0 C to give deposit of approximately 8 microns.
  • the deposit after rinsing, was immersed in a proprietary blue passivation composition for 15 seconds to give a pleasing blue tint to the electrodeposited zinc.

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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)
EP19810300833 1980-02-28 1981-02-27 Bains de zingage et additifs pour ceux-ci Withdrawn EP0037634A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8006402 1980-02-28
GB8006402 1980-02-28

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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2120501C1 (ru) * 1996-12-09 1998-10-20 Чувашский государственный университет им.И.Н.Ульянова Электролит цинкования
WO2000014305A1 (fr) * 1998-09-02 2000-03-16 Atotech Deutschland Gmbh Bain alcalin aqueux exempt de cyanure s'utilisant pour le depot par galvanisation de revetements en zinc ou en alliage de zinc
EP0987349A1 (fr) * 1998-09-15 2000-03-22 LPW-Chemie GmbH Procédé de dépôt galvanique des couches de zinc et/ou des couches d'alliages de zinc
US6238542B1 (en) 1998-09-15 2001-05-29 Thomas Helden Water soluble brighteners for zinc and zinc alloy electrolytes
US9269998B2 (en) 2013-03-13 2016-02-23 Fluidic, Inc. Concave gas vent for electrochemical cell
US9325037B2 (en) 2013-03-13 2016-04-26 Fluidic, Inc. Hetero-ionic aromatic additives for electrochemical cells comprising a metal fuel
CN106435659A (zh) * 2016-11-21 2017-02-22 江苏梦得新材料科技有限公司 一种电镀锌用光亮剂
US11664547B2 (en) 2016-07-22 2023-05-30 Form Energy, Inc. Moisture and carbon dioxide management system in electrochemical cells
US12136723B2 (en) 2016-07-22 2024-11-05 Form Energy, Inc. Mist elimination system for electrochemical cells
US12237548B2 (en) 2018-06-29 2025-02-25 Form Energy, Inc. Stack of electric batteries including series of fluidly connected unit cells
US12261281B2 (en) 2018-06-29 2025-03-25 Form Energy, Inc. Metal air electrochemical cell architecture
US12308414B2 (en) 2019-06-28 2025-05-20 Form Energy, Inc. Device architectures for metal-air batteries
US12381244B2 (en) 2020-05-06 2025-08-05 Form Energy, Inc. Decoupled electrode electrochemical energy storage system

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1381939A (en) * 1971-06-28 1975-01-29 Du Pont Acid zinc electroplating baths and the use thereof
GB1394637A (en) * 1972-09-26 1975-05-21 M & T Chemicals Inc Electrodeposition of zinc
US4045306A (en) * 1975-06-04 1977-08-30 Schering Aktiengesellschaft Electroplating zinc and bath therefor
US4093523A (en) * 1977-02-07 1978-06-06 Edward B. Wild Bright acid zinc electroplating baths
GB2009790A (en) * 1977-12-06 1979-06-20 M & T Chemicals Inc Zinc electroplating
US4166778A (en) * 1978-05-17 1979-09-04 Simeon Acimovic Cyanide-free alkaline zinc baths
US4169772A (en) * 1978-11-06 1979-10-02 R. O. Hull & Company, Inc. Acid zinc plating baths, compositions useful therein, and methods for electrodepositing bright zinc deposits

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1381939A (en) * 1971-06-28 1975-01-29 Du Pont Acid zinc electroplating baths and the use thereof
GB1394637A (en) * 1972-09-26 1975-05-21 M & T Chemicals Inc Electrodeposition of zinc
US4045306A (en) * 1975-06-04 1977-08-30 Schering Aktiengesellschaft Electroplating zinc and bath therefor
US4093523A (en) * 1977-02-07 1978-06-06 Edward B. Wild Bright acid zinc electroplating baths
GB2009790A (en) * 1977-12-06 1979-06-20 M & T Chemicals Inc Zinc electroplating
US4166778A (en) * 1978-05-17 1979-09-04 Simeon Acimovic Cyanide-free alkaline zinc baths
US4169772A (en) * 1978-11-06 1979-10-02 R. O. Hull & Company, Inc. Acid zinc plating baths, compositions useful therein, and methods for electrodepositing bright zinc deposits

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2120501C1 (ru) * 1996-12-09 1998-10-20 Чувашский государственный университет им.И.Н.Ульянова Электролит цинкования
WO2000014305A1 (fr) * 1998-09-02 2000-03-16 Atotech Deutschland Gmbh Bain alcalin aqueux exempt de cyanure s'utilisant pour le depot par galvanisation de revetements en zinc ou en alliage de zinc
US6652728B1 (en) 1998-09-02 2003-11-25 Atotech Deutschland Gmbh Cyanide-free aqueous alkaline bath used for the galvanic application of zinc or zinc-alloy coatings
EP0987349A1 (fr) * 1998-09-15 2000-03-22 LPW-Chemie GmbH Procédé de dépôt galvanique des couches de zinc et/ou des couches d'alliages de zinc
US6238542B1 (en) 1998-09-15 2001-05-29 Thomas Helden Water soluble brighteners for zinc and zinc alloy electrolytes
US9325037B2 (en) 2013-03-13 2016-04-26 Fluidic, Inc. Hetero-ionic aromatic additives for electrochemical cells comprising a metal fuel
US9269998B2 (en) 2013-03-13 2016-02-23 Fluidic, Inc. Concave gas vent for electrochemical cell
US11664547B2 (en) 2016-07-22 2023-05-30 Form Energy, Inc. Moisture and carbon dioxide management system in electrochemical cells
US12136723B2 (en) 2016-07-22 2024-11-05 Form Energy, Inc. Mist elimination system for electrochemical cells
CN106435659A (zh) * 2016-11-21 2017-02-22 江苏梦得新材料科技有限公司 一种电镀锌用光亮剂
US12237548B2 (en) 2018-06-29 2025-02-25 Form Energy, Inc. Stack of electric batteries including series of fluidly connected unit cells
US12261281B2 (en) 2018-06-29 2025-03-25 Form Energy, Inc. Metal air electrochemical cell architecture
US12308414B2 (en) 2019-06-28 2025-05-20 Form Energy, Inc. Device architectures for metal-air batteries
US12381244B2 (en) 2020-05-06 2025-08-05 Form Energy, Inc. Decoupled electrode electrochemical energy storage system

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