GB2351084A - Zinc and zinc alloy electroplating additives and electroplating methods - Google Patents

Zinc and zinc alloy electroplating additives and electroplating methods Download PDF

Info

Publication number
GB2351084A
GB2351084A GB9913968A GB9913968A GB2351084A GB 2351084 A GB2351084 A GB 2351084A GB 9913968 A GB9913968 A GB 9913968A GB 9913968 A GB9913968 A GB 9913968A GB 2351084 A GB2351084 A GB 2351084A
Authority
GB
United Kingdom
Prior art keywords
zinc
polymer
formula
alloys
polymer additive
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Withdrawn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
GB9913968A
Other versions
GB9913968D0 (en
Inventor
Trevor Pearson
Alan Swales
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.)
MacDermid Performance Solutions UK Ltd
Original Assignee
MacDermid Canning PLC
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 MacDermid Canning PLC filed Critical MacDermid Canning PLC
Priority to GB9913968A priority Critical patent/GB2351084A/en
Publication of GB9913968D0 publication Critical patent/GB9913968D0/en
Priority to BR0005005-9A priority patent/BR0005005A/en
Priority to CNB00800210XA priority patent/CN1198001C/en
Priority to DE60010591T priority patent/DE60010591T2/en
Priority to AT00905169T priority patent/ATE266750T1/en
Priority to CA2329802A priority patent/CA2329802C/en
Priority to AU26799/00A priority patent/AU764300B2/en
Priority to PCT/GB2000/000592 priority patent/WO2000050669A2/en
Priority to KR1020007011878A priority patent/KR20010043020A/en
Priority to ES00905169T priority patent/ES2215607T3/en
Priority to US09/674,105 priority patent/US6706167B1/en
Priority to JP2000601228A priority patent/JP3946957B2/en
Priority to EP00905169A priority patent/EP1075553B1/en
Priority to ARP000100780A priority patent/AR026110A1/en
Publication of GB2351084A publication Critical patent/GB2351084A/en
Withdrawn legal-status Critical Current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
    • C25D3/56Electroplating: Baths therefor from solutions of alloys
    • C25D3/565Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of zinc
    • 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

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

A polymer additive for alkaline zinc and zinc alloy electrodepositing media and processes comprises the reaction product of one or both of <SL> <LI>(i) a first di-tertiary amine (containing an amide functional group, such as N,N'-bis[3-(dimethylamino)propyl]urea) of the formula: <EMI ID=1.1 HE=21 WI=74 LX=989 LY=193 TI=CF> where R' represents <EMI ID=1.2 HE=9 WI=33 LX=1317 LY=420 TI=CF> and q is 2 to 6,<BR> R represents CH<SB>3</SB> or C<SB>2</SB>H<SB>5</SB>, and each R may be the same or different<BR> and m is 2 to 4, and<BR> a second di-tertiary amine containing an alkyl group, such as N,N,N'N'-tetramethyl -1,6,hexane diamine, N,N,N',N'-tetramethyl-1,3-propane diamine, N,N,N',N'-tetramethyl-1,3 butane diamine of the formula : <EMI ID=1.3 HE=39 WI=60 LX=1077 LY=843 TI=CF> where B is C<SB>9</SB>H<SB>2g+1</SB> and g = 0 or an integer the respective B groups being the same or different, and f = 0 o an integer, and<BR> R'' represents CH<SB>3</SB> or C<SB>2</SB>H<SB>5</SB> and each R'' may be the same or different,<BR> with<BR> <LI>(ii) a di-halo alkane (such as 1,4-dichlorobutane, 1,5-dichloropentane, 1,6-dichlorohexane, 1,3-dichlorobutane) of the formula :<BR> <BR> A - (CH<SB>2</SB>)<SB>n</SB> - A<BR> <BR> where A represents a halogen atom and n is at least 2. </SL> The resulting polymer preferably has the general structure. <EMI ID=1.4 HE=33 WI=91 LX=864 LY=1941 TI=CF> <PC>(2x + 2y) A<SP>-</SP><BR> Where: 0 & x & 1<BR> ```0 & y & 1 and: either (x or y) or (x and y) = 1<BR> A process for electrodepositing zinc and or zinc alloys is also disclosed.

Description

2351084 Zinc and Zinc Alloy Electroplating Additives an Electroplating
Methods The present invention relates generally to improvements 5 in the electrodeposition of zinc and zinc alloys from aqueous alkaline plating baths and to new additives for use in such electrodeposition processes.
Electrodeposition of zinc and zinc alloys, based for example on sodium zincate, has been known for many years.
It is not possible to produce a commercially acceptable deposit from a simple sodium zincate electrolyte as the deposit is powdery and dendritic. For this reason, various additives have been proposed to provide improved deposition, such as cyanides (which have obvious is environmental problems) and polymers of amines and epichlorohydrin which act as grain refining additives. These polymers are limited to usage in baths having relatively low concentrations of zinc because it is not possible to prevent uncontrolled deposition of zinc at higher metal concentrations. Also, electroplating processes using these additives tend to have poor cathode efficiency, a narrow bright range, a narrow operating window and tend to produce pitted and "burnt" deposits.
More recently, additives have been proposed which allow higher zinc concentrations to be used, which have significantly reduced burning and pitting and which allow a wider range of operating parameters. Further, the additives enable an excellent deposit distribution (that is, evenness of the deposit across the article being plated, irrespective of its shape in particular areas). This maximises the efficiency of zinc usage. These 2 additives are based generally on polyquaternary amine compounds and are described in US 5 435 898 and US 5 405 523, which also provide further discussion of the prior art.
US 5 435 898 describes polymers for use as additives in the electrodeposition of zinc and zinc alloys, the polymers having the general formula:
R, Y R3 1 N"- (CH2) 3 - 1"HC-1"'H_(CH2) 3 -N±Rs --- 2nCl R2 R4 n is R, to R4 may be the same or different and are, inter alia, methyl, ethyl or isopropyl and Y may be S or 0. R. is an ether linkage such as (CH2)2-0(CH2) 2 US 5 405 523 claims ureylene quaternary ammonium polymers in general as brightening agents in zinc alloy electroplating baths. The preferred and exemplified polymers include units of the general formula:
R A R - N+ - (C112)x - NH - (CH2) x - N - R where A may be 0, S or N and R may be, inter alia, methyl, ethyl or isopropyl. In the preferred polymers, these units are linked by units derived from, for example a bis(2-haloethyl) ether, a (halomethyl) oxirane or a 2, 21 -(ethyl enedioxy) - diethylhal ide. Ethylene dihalides such 3 as ethylene dichloride and ethylene dibromide are also suggested but not exemplified.
Further known additives are polycationic compositions based on polymerisation of dimethyl-diallyl ammonium 5 chloride with sulphur dioxide as described in DE 19,509,713.
However, the overall cathodic efficiency of these processes can be low and the resultant deposits may be unsatisfactory in terms of brightness and levelling.
The present invention provides improved polymers for use as additives in the electrodeposition of zinc and zinc. alloys. In particular, it has been found that by avoiding an ether-type linkage such as R. in the prior art above, a brighter deposit may be obtained which is also easier is subsequently to apply conversion coatings.
The present invention is thus concerned with electrodeposition on a variety of electrically conducting substrates in a medium which may provide improved cathode efficiency and/or improved brightness and/or a more stable finish which is suitable for further treatment. Suitable substrates include iron and all ferrous-based substrates (including both iron alloys and steels), aluminium and its alloys, magnesium and its alloys, copper and its alloys, nickel and its alloys, and zinc and its alloys. Aluminium and its alloys and ferrousbased substrates are particularly preferred substrates, with steels being most preferred.
In its broadest sense, the invention provides polymers for use as additives in the electrodepostion of zinc and 4 zinc alloys, and processes employing the polymers,the polymers being obtained by the reaction of one or both of:
(a) a di-tertiary amine containing an amide functional group and (b) a di-tertiary amine containing an alkyl group, with (c) a di-halo alkane, to form a random co-polymer.
The present invention also relates to a method of coating' an electrically conducting substrates; with zinc. or zinc alloy by electrodeposition from a bath medium comprising of an effective amount of the reaction product of one or both of: (a) di-tertiary amine containing an amide functional group and (b) a ditertiary amine containing an alkyl group, with (c) a di-halo alkane, to torm a random co-polymer, a source of zinc ions and optionally additional metal ions of one of more alloying metals, and a chelating agent to render the ions soluble.
The di-tertiary amine (a) containing an amide functional group in the polymer of the invention has the general formula:
1 R R N(CH2)m -NH-RINH-(CH2),-N (1) 1 R.--- where R' represents 0 0 0 c or C- (CH,) q-C and q is 2 to 6, R i s CH3 or C2H. and each R may be the same or different, and m is 2 to 4.
An example of a suitable ditertiary amine of Formula (1) is N,NI-bis[3(dimethylamino)propylI urea.
The ditertiary amine (b) containing an alkyl g,,coup has the general formula:
R" B N R' HC---- (CH2) f --- CI is R" N W' / where B is C.H2.., and 9 = 0 or an integer the respective B groups being the same or different, and f 0 o an integer, and W' is CH3 or C2H. and each W' may be the same or different.--Thus, the amine groups may be terminal or branched with respect to the alkyl chain portion. Preferably, however, 6 the amine groups are terminal, as indicated by the general formula:
R to R" 1 N - (CH2) p N (3) R le R where W' is CH3 or C2H. and each W' may be the same or different, and p is at least 2.
Examples of suitable di-tertiary amines of Formula (2)include N,N,NI,Nltetramethyl-1,6-hexanediamine, N,N,NIN1 -tetramethyl-1,3-propane diamine and N,N,N1,NI tetramethyl1,3 butane diamine.
The dihaloalkane (c) may be represented by the general f ormul a:
A - (C,_12) n - A (4) is where A represents a halogen atom, especially chlorine or bromine and most preferably chlorine, and n is at least 2, provided that if the monomer of formulas (2) or (3) above is absent, n is at least 3.
Examples of the dihaloalkanes of formula (4) include 1,4- dichlorobutane, 1,5-dichloropentane, 1,6-dichlorohexane and 1,3- dichlorobutane. The latter is believed to result in a polymer additive which is less effective than those dihaloalkanes where the halogen atoms are in terminal_ positions only.
The upper limit of n (formula (4)) p (formula (3)) or f and g (formula (2)) respectively is determined.by the the 7 need for the resultant polymer to be soluble in the electroplating bath. In practical terms, it is envisaged that the upper limit of n and p respectively will be about 8, that f will be not more than 6 and that g will not be more than 3 as higher values produce polymers of insufficient solubility.
The resultant polymer additive according to the present invention may be represented by the formula:
R R R" W' N±(CH -NHRl-NH- -N±--- -(CH l± (CH - br ------ 2) (C'42) 2) rt- 2) p (CH2) n - 1 1 _ R R X- - x _ C - C v Y z (2x + 2y) A- is Where: 0: X < 1 0 < y < 1 and either (x or y) or (x and y) z is at least 2 and when y=O, n is at least 3.
In practice, it may be difficult to produce polymers 20 where n and p both have a value of 2 and also x is 0. For this reason, when x=o, it is preferred that the sum n+p is at least 6.
In the polymer additive of the invention the di-tertiary amine unit containing an amide functional group may be 25 absent (i.e. when x=O) or the di-tertiary amine unit 8 containing an alkyl group may be absent (i.e. y=o), but one or other of these units must be present. Preferably, both units are present. The polymer of the invention when both the above mentioned units are present is a random co-polymer such that the respective di-tertiary amine units appear in random sequence (in all cases linked by the di-halo alkane residue).
The absolute value of z is not specified as the polymer of the invention will normally comprise polymer molecules of a range of molecular weights. For individual polymer molecules, z will generally be at least 4 to 20 and may be as high as 100 or more.
Also, the molar ratio in the polymer of the di-tertiary amine units derived from formulas (1) and (2) is respectively may be selected as desired in order to achieve particular properties. Thus, a polymer in which y=0 results in a zinc electrodeposition process producing a very bright deposit with good distribution (even coating) but the cathode efficiency is not as high as may be desirable. A polymer where both x and y are greater than 0 provides good brightness and good distribution, together with good cathode efficiency. Preferably, the molar ratio of the di-tertiary amines derived from formulae (1) and (2) is in the range of 25:75 to 75:25.
More preferably, the ratio is 50:50 to 75:25, and most especially 62.5:37.5.
For the di-tertiary amine of formula (1), R' is preferably 0 11 C, but when R' is 9 0 0 C - (CH,) q - c q is preferably 4 to 6. Further R (irrespective of R') is particularly preferably C113.
In the di-tertiary amine represented by formula (2) W' is preferably CH3 and f is pref erably 2 to 4 so that in formula (3), p is preferably 4 to 6.
For the dihaloalkane of formula (4), n is preferably in the range of 4 to 6.
The following examples are illustrative of preparation techniques for polymers according to the invention.
EXAMPLE 1
N, NI -Bis [3 - (dimethylamino) propyl 1 urea (15. 0 grams) 1, 4 dichlorobutane (8.3 grams) and water (23.3 grams) are introduced into to a reaction flask equipped with a reflux condenser, thermometer and stirrer. The reagents are stirred and heated to reflux until the reaction progresses sufficiently towards completion. A reflux of 4 to 5 hours or more is suitable. The resulting liquid is allowed to cool to room temperature giving an aqueous solution of the desired product. In these examples, 100% completion of the reaction may not be achievable or necessary and the reflux time may be varied accordingly.
EXAMPLE 2
N,N' -Bis [3- (dimethylamino) proply] urea (6.3 grams), N,N, NI,Nltetramethyl-1,6-hexanediamine (4.7 grams), 1,4- dichlorobutane (6.9 grams) and water (18.0 grams) are introduced into a reaction flask equipped with a reflux condenser, thermometer and stirrer. The reagents are stirred and heated to reflux for a sufficient time to achieve the required degree of completion of the reaction, typically at least 5 hours. The resulting liquid is allowed to cool to room temperature giving an aqueous solution of the desired product.
EXAMPLE 3
N,N,NI,Nl-tetramethyl-1,6-hexanediamine (10.0 grams), 1,5-dichloropentane (8.1 grams) and water (18.1 grams) are introduced into to a reaction flask equipped with a reflux condenser, thermometer and stirrer. The reagents are stirred and heated to reflux for a sufficient time to is achieve the required degree of completion of the reaction, typically at least 7 hours. The resulting liquid is allowed to cool to room temperature giving an aqueous solution of the desired product.
EXAMPLE 4
N, N1 -B i s [ 3 - (dimethylamino) propyl 1 urea (9. 0 grams), N, N, N', Nl-tetramethyl-1,3-propanediamine (5.1 grams), 1,6dichlorohexane (12.1 grams) and water (26.2 grams) are introduced into to a reaction flask equipped with a reflux condenser, thermometer and stirrer. The reagents are stirred and heated to reflux for a sufficient time to achieve the required degree of completion of the. reaction, typically at least 8-10 hours. The resulting liquid is allowed to cool to room temperature giving an aqueous solution of the desired product.
The polymer additives according to the invention can provide excellent results in zinc or zinc alloy electroplating processes when used on their own. Further benefits may be obtained by combination of the polymer additive of the invention with known further additives, such as those indicated in the groups below:
Group 1: Polymers according to the invention - Group 2: Additives selected from the following: Silicate, tartrate, gluconate, heptonate ok other hydroxy acids Group 3: N-Benzyl Niacin and/or bath soluble 'aromatic aldehydes and their bisulphite adducts Group 4: Imidazole/epihalohydrin polymers or other amine/epihalohydrin polymers Preferably, one compound from each group is present in the plating bath medium in an effective amount.
The following examples are illustrative of zinc and zinc alloys electroplating media and processes employing the polymer additives of the present invention. The following examples relate to electrodepostion experiments which were performed on mild steels, i.e. a ferrous based substrate. However, the procedures described in these is examples are equally suitable for electrodeposition onto aluminium and its alloys, magnesium and its alloys, copper and its alloys, nickel and its alloys, and zinc and its alloys.
EXAMPLE A
12 An aqueous electrolyte suitable for plating zinc was prepared containing 12 g/1 Zinc (as metal) and 135 g/1 NaOH. A Hull cell test was performed on this electrolyte at 1A for 10 minutes. The resultant deposit was black and powdery and was not suitable for commercial use. 3 ml/1 of the product formed in example 1 was added to the electrolyte. A 1A Hull cell test now gave a semi-bright deposit of zinc at current densities of 0.5 to 5 A/dm2.
EXAMPLE B
An aqueous electrolyte suitable for plating zinc was' prepared containing 12 g/1 Zinc (as metal) and. 135 9/1 NaOH. 3 ml/l of the product of example 2 was added and a Hull cell test was performed. A semi-bright deposit was formed at current densities of 0.1 to 4 A/dm2.
EXAMPLE C
An aqueous electrolyte suitable for plating zinc was prepared containing 12 g/1 Zinc (as metal) and 135 g/1 NaOH. 3 ml/l of the product of example 3 was added and a Hull cell test was performed. A dull but fine grained deposit was formed at current densities of 0.05 to 5 A/dM2.
EXAMPLE D
An aqueous electrolyte suitable for plating zinc was prepared containing 12 g/1 Zinc (as metal) and 135 g/1 NaOH. 3 ml/l of the product of example 4 was added and aHull cell test was performed. A semi-bright deposit was formed at current densities of 0.1 to 4 A/dm2.
13 EXAMPLE E
An aqueous electrolyte suitable for plating zinc was prepared containing 12 g/1 Zinc (as metal) and 135 g/1 NaOH. 3 ml/1 of the product of example 2,0.5 ml/l of an imidazole/epichlorohydrin polymer (Lugalvan ES 9572 from BASF),0.05 g/1 of N-Benzyl Niacin and 8 g/1 of sodium silicate was added to the electrolyte. A 1 amp-Hull cell test performed on this electrolyte produced a fully bright lustrous deposit over the entire current density range of the Hull cell panel. The thickness of the deposit obtained on this panel was at least 25% greater than that obtained from a comparative panel prodilced from an electrolyte prepared as above but substituting an equivalent concentration of Mirapol WT (a polymer as described in US 5,435,898) for the product of example 2.
EXAMPLE F
An aqueous electrolyte suitable for plating zinc was prepared containing 12 g/1 Zinc (as metal) and 135 g/1 NaOH. 3 ml/l of the product of example 2,0.5 ml/1 of an imidazole/epicholohydrin polymer (Lugalvan ES 9572),0.05 g/1 of N-Benzyl Niacin and 1 g/1 of sodium potassium tartrate was added to the electrolyte. A 1 amp Hull cell test performed on this electrolyte produced a fully bright lustrous deposit over the entire current density range of the Hull cell panel.
EXAMPLE G
An aqueous electrolyte suitable for plating zinc was prepared containing 12 9/1 Zinc (as metal) and 135 g/1 NaOH. 3 ml/l of the product of example 3,0.5 ml/1 of an 14 imidazole/epichlorohydrin polymer (Lugalvan ES 9572), 0. 05 g/1 of N- Benzyl Niacin and 8 g/1 of sodium silicate was added to the electrolyte. A 1 amp Hull cell test performed on this electrolyte produced a fully bright lustrous deposit over the current density range of 0.05 to 4 A/dM2.
EXAMPLE H
An aqueous electrolyte suitable for plating a zin.c/iron alloy was prepared containing 12 g/1 zinc (as metal), 135 g/1 NaOH, 60 9/1 sodium heptonate and 100 mg/1 of iron.- 3 ml/l of the product of example 2,0.5 ml/l of an imidazole/epichlorohydrin polymer (Lugalvan ES 9572) and 0.05 9/1 of N- Benzyl Niacin was added to the electrolyte. A 1 amp Hull cell test performed on this electrolyte is produced a fully bright lustrous deposit over the entire current density range of. the Hull cell panel. Passivation of the Hull cell panel in a chromating bath containing chromic acid, sulphuric acid, phosphoric acid and other inorganic salts produced a uniform black coating thus indicating uniform co-deposition of iron over the Hull cell panel.
EXAMPLE I
An aqueous electrolyte suitable for plating a zinc/ cobalt/iron alloy was prepared containing 12 g/1 Zinc (as metal), 135 g/1 NaOH, 60 g/1 sodium heptonate and 50 mg/1 of iron and 80 mg/1 cobalt. 3 ml/l of the product of example 2,0.5 M1/1 of an imidazole/epichlorohydrin polymer (Lugalvan ES 9572) and 0.05 g/1 of N-Benzyl Niacin was added to the electrolyte. A 1 amp Hull cell test performed on this electrolyte produced a fully bright lustrous deposit over the entire current density range of the Hull cell panel. Passivation of the Hull cell panel in a chromating bath containing chromic acid, sulphuric acid, phosphoric acid and other inorganic salts produced a uniform black coating thus indicating uniform co-deposition of cobalt and iron over the Hull cell panel. Subsequent analysis of the deposit by energy dispersive Xray analysis showed a cobalt concentration 10 of 0.4% over a wide range of current densities.
EXAMPLE J
An aqueous electrolyte suitable for plating zinc was prepared containing 12 g/1 Zinc (as metal) and 135 g/1 NaOH. 3 ml/l of the product of example 2,0.5 ml/l of an is imidazole/epichlorohydrin polymer (Lugalvan ES 9572)), 0.1 g/1 of Veratraldehyde (3,4.-dimethoxybenzaldehyd. e) and 19/1 of sodium potassium tartrate was added to the electrolyte. A 1 amp Hull cell test performed on this electrolyte produced a bright but slightly hazy deposit 20 over the entire current density range of the Hull cell panel.
16 The present invention further relates to a polymer additive for an alkaline zinc or zinc alloy electroplating bath medium comprising the reaction product of one or both of:
(i) a first di-tertiary amine of the formula:
R R N - (CH2), - NH R NH - (CH,) m N (1) R/ \ R where R' represents 0 or 0 0 /1 11 kk 1 c C - (CH2) q - c and q is 2 to 6, R represents CH3 or C2H. and each R may be the same or different and m is 2 to 4, and is a second di-tertiary amine of the formula:
R" B N R" HC ---- (CH2) f --- CH R" B "I / N W' / 17 where B is C.H29+1 and g = 0 or an integer the respective B groups being the same or different, and f = 0 or an integer, and R" represents CH. or CH, and each R" may be tile same or different, with (ii) a di-halo alkane of the formula:
A - (CH2) n - A (4) where A represents a halogen atom and n is at least 2, provided that when the monomer of formula (2) or (3) is absent, n is at least 3, and provided that the dihalo alkane is not 1,4 dichlorobutane when the amine is N,N1 bis [3-(amino dimethyl) propyll urea or N, N, NI, NI tetramethyl - 1,6 - diamine hexane, or 1,6 - dibromohexane when the amine is N, NI - bis [3-(amino dimethyl) propyll urea.
The present invention also relates to a process for electrodepositing zinc and/or zinc alloys on a conductive substrate which process comprises contacting the substrate with the bath medium of any of claims 16 to 22 and electrodepositing zinc or zinc alloys on the substrate, provided that in the case of an aluminium or aluminium alloy substrate the dihalo alkane is not 1,4 dichlorobutane when the amine is N, NI - bis [3-(amino dimethyl) propyll urea or N, N, NI, NI - tetramethyl 1, 6 - diamine hexane, or 1, 6 - dibromohexane when the amine is N, NI - bis [3- (amino dimethyl) propyll urea.
18

Claims (31)

  1. A polymer additive for an alkaline zinc or zinc alloy electroplating bath medium comprising the reaction product of one or both of:
    (i) a first di-tertiary amine of the formula:
    R R N - (CH2) m - NH - R' - NH - (CH2) M - N, (1) R/ \ R where R' represents 0 or 0 0.
    c C - (CH2) q - c and q is 2 to 6, R represents CH3 or C2H. and each R may be the same or different and m is 2 to 4, and a second di-tertiary amine of the formula:
    R" B N W' HC---- (CH2) f --- CH R" -1,' / N W' / --- 19 where B is C.H2.+1 and 9 = 0 or an integer the respective B groups being the same or different, and f = 0 or an integer, and R" represents CH3 or C2H. and each C may be the same or different, with (ii) a di-halo alkane of the formula:
    A - (CH2) n - A (4) where A represents a halogen atom and n is at least 2, provided that when the monomer of formula (2) or (3) is absent, n is at least 3.
  2. 2. A polymer additive as claimed in claim 1 wherein the second ditertiary amine has the general formula:
    R" R" is N - (CH2) p - N R" W' where W' is as defined above and p is at least 2.
  3. 3. A polymer additive as claimed in claim 2 wherein p is not more than 8.
  4. 4. A polymer additive as claimed in claim 1, 2 or 3 comprising a random co-polymer of the general formula:
    1 R 1 R 1 W', R 91 N'- (CH2) m- NH R' - NH (H1),,, (CH2) n L N+ - - (CH2) n R _R _ _ X - X R" - - - R" Y Yz (2x + 2y) A- Where: 0:5 X < 1 0:5 y < 1 and. either (x or y) or (x and y) = 1 z is at least 2 and when y=O, n is at least 3.
  5. 5. A polymer additive as claimed in any of claims 1 to 4 wherein n is not more than 8.
  6. 6. A polymer additive as claimed in any of claims 1 to 15 5 wherein f is not more than 6 and/or g is not more than 3.
  7. 7. A polymer additive as claimed in any of claims 1 to 6 where R is CH3.
  8. 8. A polymer additive as claimed in any preceding claim wherein C is CH3.
  9. 9. A polymer as claimed in any preceding claim wherein---. f is 2 to 4.
  10. 10. A polymer as claimed in claim 2 or 3 wherein p is 4 to 6.
    21
  11. 11. A polymer as claimed in any of claims 1 to 7 wherein R' is 0 0 U W C - (CH2) q - C and q is 4 to 6.
  12. 12. A polymer as claimed in any preceding claim wherein moieties derived from the first di-tertiary amine and the second di-tertiary amine are present in the ratio of from 25:75 to 75:25.
  13. 13. A polymer additive as claimed in any of claims 1 to wherein the first di-tertiary amine is N,NI bis[3-(dimethylamino)propyllurea.
  14. 14. A polymer additive as claimed in any preceding claim wherein the second di-tertiary amine is N,N,N1,N1 - tetramethyl-1,6-hexanediamine.
  15. 15. A polymer additive as claimed in any preceding claim is wherein the di-haloalkane is 1,4-dichlorobutane.
  16. 16. An aqueous alkaline zinc or zinc alloy bath medium for depositing zinc or zinc alloys comprising a source of zinc ions and, in the case of the alloy, a source of additional metal ions of the alloying metals and a suitable chelating agent to render the ions soluble and a functional amount of the polymer of any of claims 1 to 15.
  17. 17. A bath medium as claimed in claim 16 wherein the alloying metal is one or more of iron, cobalt and-- nickel.
    22
  18. 18. A bath medium as claimed in claim 16 or 17 wherein the zinc is present as sodium zincate or potassium zincate.
  19. 19. A bath medium as claimed in claim 18 wherein the zinc is present in an amount of 5 to 35 g/1 (expressed as zinc metal).
  20. 20. A bath medium as claimed in any of claims 16 to 19 wherein the alkalinity is provided by sodium hydroxide or potassium hydroxide in an amount of 50 to 200 g/1.
  21. 21. A bath medium as claimed in any of claims 16 to 20 wherein the polymer additive is present in an amount of 0.5 to 5 9/1.
  22. 22. A bath medium as claimed in any of claims 16 to 21 is further comprising an effective amount of one or more additional additives selected from one or more of the groups comprising A: silicates; B: gluconate, heptonate and tartrate; C: N-Benzyl Niacin; D: aromatic aldehydes and their bisulphite adducts;and E: amine/epihalohydrin polymers, preferably imidazole/epihalohydrin polymers.
  23. 23. A process for electrodepositing zinc and/or zinc alloys on a conductive substrate which process 23 comprises contacting the substrate with the bath medium of any of claims 16 to 22 and electrodepositing zinc or zinc alloys on the substrate.
  24. 24. A process as claimed in claim claim 23, wherein the conductive substrate is selected from the group comprising aluminium and its alloys, ferrous based substrates, magnesium and its alloys, copper and its alloys, nickel and its alloys, and zinc and its alloys.
  25. 25. A process as claimed in claim 24, wherein the conductive substrate is steel.
  26. 26. The use of the polymer of any of claims 1 to 15 as an additive in an aqueous zinc or zinc alloy bath medium for electrodepositing zinc or zinc alloy.
  27. 27. A polymer additive as claimed in claim 1 substantially as herein before described.
  28. 28. A polymer additive substantially as herein before described with reference to any of Examples 1 to 4.
  29. 29. A zinc or zinc alloy bath medium for electrodepositing zinc or zinc alloy substantially as herein before described with reference to any of Examples A to J.
  30. 30. A polymer additive for an alkaline zinc or zinc alloy electroplating bath medium comprising the reaction product of one or both of:
    (i) a first di-tertiary amine of the formula:
    24 R R N - (CH2) in - NH - R' - NH - (CH2) m - N (1) R/ \ R where R' represents 0 or 0 0 11 11 c c (CH2) q - c and q is 2 to 6, R represents CH3 or C2H, and each R may be the same or different and m is 2 to 4, and a second di-tertiary amine of the formula:
    we B N C HC ---- (CH2) f --- CH is R" B "I / N W' / where B is C.H29+1 and g = 0 or an integer the respective B groups being the same or different, and f = 0 or an integer, and W' represents CH3 or C2H5 and each R" may be the-- same or different, with (ii) a di-halo alkane of the formula:
    A - (CH2) n - A (4) where A represents a halogen atom and n is at least 2, provided that when the monomer of formula (2) or (3) is absent, n is at least 3, and provided that the dihalo alkane is not 1,4 dichlorobutane when the amine is N,N, bis [3 (amino dimethyl) propyll urea or N,N' NI,, NI - tetramethyl - 1,6 - phidmine hexane, or 1,6 dibromohexane when the amine is N, NI bis [3 (amino dimethyl) propyll urea.
  31. 31. A process for electrodepositing zinc and/or zinc alloys on a conductive substrate which process comprises contacting the substrate with the bath is medium of any of claims 16 to 22. 0 and electrodepositing zinc or zinc alloys on the substrate, provided that in the case of an aluminium or aluminium alloy substrate the dihalo alkane is not 1,4 dihlorobutane when the amine is N, NI - bis D-(amino dimethyl) propyll urea or N, N, NI, NI - tetramethyl - 1,6 - diamine hexane, or 1, 6 - dibromohexane when the amine is N, NI - bis [3 (amino dimethyl) propyll urea.
GB9913968A 1999-02-25 1999-06-16 Zinc and zinc alloy electroplating additives and electroplating methods Withdrawn GB2351084A (en)

Priority Applications (14)

Application Number Priority Date Filing Date Title
GB9913968A GB2351084A (en) 1999-06-16 1999-06-16 Zinc and zinc alloy electroplating additives and electroplating methods
EP00905169A EP1075553B1 (en) 1999-02-25 2000-02-21 Zinc and zinc alloy electroplating additives and electroplating methods
AU26799/00A AU764300B2 (en) 1999-02-25 2000-02-21 Zinc and zinc alloy electroplating additives and electroplating methods
KR1020007011878A KR20010043020A (en) 1999-02-25 2000-02-21 Zinc and zinc alloy electroplating additives and electroplating methods
DE60010591T DE60010591T2 (en) 1999-02-25 2000-02-21 ZINC AND ZINC ALLOY ELECTROPLATING ADDITIVES AND ELECTROPLATING METHOD
AT00905169T ATE266750T1 (en) 1999-02-25 2000-02-21 ZINC AND ZINC ALLOY- ELECTRO PLATING ADDITIVES AND ELECTRO PLATING PROCESSES
CA2329802A CA2329802C (en) 1999-02-25 2000-02-21 Zinc and zinc alloy electroplating additives and electroplating methods
BR0005005-9A BR0005005A (en) 1999-02-25 2000-02-21 Polymer additive for alkaline zinc or zinc alloy electroplating bath media, alkaline zinc or zinc alloy bath media, process for electroplating zinc and / or zinc alloys on a conductive substrate, and use of the polymer
PCT/GB2000/000592 WO2000050669A2 (en) 1999-02-25 2000-02-21 Zinc and zinc alloy electroplating additives and electroplating methods
CNB00800210XA CN1198001C (en) 1999-02-25 2000-02-21 zinc and zinc alloy electroplating additives and electroplating methods
ES00905169T ES2215607T3 (en) 1999-02-25 2000-02-21 USEFUL ASSISTANTS FOR ZINC ELECTRODEPOSITION AND ZINC ALLOYS AND ELECTRODEPOSITION PROCEDURES.
US09/674,105 US6706167B1 (en) 1999-02-25 2000-02-21 Zinc and zinc alloy electroplating additives and electroplating methods
JP2000601228A JP3946957B2 (en) 1999-02-25 2000-02-21 Zinc and zinc alloy electroplating additive and electroplating method
ARP000100780A AR026110A1 (en) 1999-02-25 2000-02-23 A POLYMERIC ADDITIVE FOR A BATH TO ELECTRODEPOSITAR ZINC AND / OR ZINC ALLOYS, A BANK THAT INCORPORATES IT AND A PROCESS FOR ELECTRODEPOSITAR ZINC AND ZINC ALLOCATIONS IN SUCH BATH

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB9913968A GB2351084A (en) 1999-06-16 1999-06-16 Zinc and zinc alloy electroplating additives and electroplating methods

Publications (2)

Publication Number Publication Date
GB9913968D0 GB9913968D0 (en) 1999-08-18
GB2351084A true GB2351084A (en) 2000-12-20

Family

ID=10855427

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9913968A Withdrawn GB2351084A (en) 1999-02-25 1999-06-16 Zinc and zinc alloy electroplating additives and electroplating methods

Country Status (1)

Country Link
GB (1) GB2351084A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2367825A (en) * 2000-07-20 2002-04-17 Macdermid Plc Zinc and zinc alloy electroplating additives and electroplating methods
WO2007045650A2 (en) * 2005-10-18 2007-04-26 Basf Se Aqueous, alkaline, cyanide-free bath for electrodepositing zinc and zinc alloy coatings
EP2175048A1 (en) * 2008-10-13 2010-04-14 Atotech Deutschland Gmbh Metal plating composition for deposition of tin-zinc alloys onto a substrate

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1507096A (en) * 1976-04-09 1978-04-12 Canning & Co Ltd W Electro-deposition of zinc
US5405523A (en) * 1993-12-15 1995-04-11 Taskem Inc. Zinc alloy plating with quaternary ammonium polymer
WO1999031301A1 (en) * 1997-12-12 1999-06-24 Wm. Canning Ltd. Method for coating aluminium products with zinc

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1507096A (en) * 1976-04-09 1978-04-12 Canning & Co Ltd W Electro-deposition of zinc
US5405523A (en) * 1993-12-15 1995-04-11 Taskem Inc. Zinc alloy plating with quaternary ammonium polymer
WO1999031301A1 (en) * 1997-12-12 1999-06-24 Wm. Canning Ltd. Method for coating aluminium products with zinc

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2367825A (en) * 2000-07-20 2002-04-17 Macdermid Plc Zinc and zinc alloy electroplating additives and electroplating methods
GB2367825B (en) * 2000-07-20 2004-04-07 Macdermid Plc Zinc and zinc alloy electroplating additives and electroplating methods
WO2007045650A2 (en) * 2005-10-18 2007-04-26 Basf Se Aqueous, alkaline, cyanide-free bath for electrodepositing zinc and zinc alloy coatings
WO2007045650A3 (en) * 2005-10-18 2007-06-14 Basf Ag Aqueous, alkaline, cyanide-free bath for electrodepositing zinc and zinc alloy coatings
EP2175048A1 (en) * 2008-10-13 2010-04-14 Atotech Deutschland Gmbh Metal plating composition for deposition of tin-zinc alloys onto a substrate

Also Published As

Publication number Publication date
GB9913968D0 (en) 1999-08-18

Similar Documents

Publication Publication Date Title
CA2329802C (en) Zinc and zinc alloy electroplating additives and electroplating methods
US5435898A (en) Alkaline zinc and zinc alloy electroplating baths and processes
US4983263A (en) Zincate type zinc alloy electroplating bath
JPH0312157B2 (en)
EP1315849B1 (en) Zinc and zinc alloy electroplating methods
EP2350355B1 (en) Zinc alloy electroplating baths and processes
CA2073478C (en) Electroplating composition and process
GB2351084A (en) Zinc and zinc alloy electroplating additives and electroplating methods
AU4768100A (en) Alloy plating
JP3486087B2 (en) Plating bath and plating process for alkaline zinc or zinc alloy
Rajendran et al. The electrodeposition of zinc-nickel alloy from a cyanide-free alkaline plating bath
JPS62287092A (en) Zinc-nickel alloy plating bath
JP4855631B2 (en) Zinc and zinc alloy electroplating additive and electroplating method
MXPA00010441A (en) Zinc and zinc alloy electroplating additives and electroplating methods
JP3526947B2 (en) Alkaline zinc plating
JP2577689B2 (en) Zincate type zinc alloy plating bath
JPH11501699A (en) Solution for electrolytic deposition of zinc or zinc alloy coatings
EP0492790A2 (en) Electroplating composition and process

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)