[0001] The present invention relates to an electrolytic process for coating a metal element
with a layer of brass, the metal element thus coated and the use of some metal elements
thus coated in reinforcing structures of articles made of vulcanized elastomeric material.
[0002] More in particular, the present invention relates to the electrolytic codeposition
of a layer of copper and zinc on a metal element such as, for example, a steel wire.
[0003] It is known that some articles of manufacture made of vulcanized elastomeric material
are reinforced by embedding suitable metal structures in an elastomeric matrix. Generally,
said metal structure is made of steel wires and/or cords.
[0004] However, steel, that is the preferred material due to its mechanical properties,
has the disadvantage of not adhering sufficiently to the vulcanized elastomeric material.
In order to obtain a good adhesion to the elastomeric material the steel is therefore
usually coated with a layer of a suitable material. The preferred coating material
is brass. In this case adhesion is enhanced by the formation, during the vulcanizing
process, of disulfide bridges (-S-S-) between the elastomeric matrix and the copper
that coats, as a component of brass, the reinforcing metal element.
[0005] The brass layer on the metal element must be as compact and homogeneous as possible
both to ensure a uniform formation of disulfide bridges, and thus a uniform adhesion
of the elastomeric matrix to the reinforcing metal structure, and to prevent the triggering
of corrosive reactions in the possible areas of the reinforcing metal structure that
are not sufficiently coated.
[0006] In fact, when adhesion is not sufficiently uniform, it occurs, right from the start
of use, some detachements of the elastomeric matrix from the reinforcing metal structure
that propagate rapidly along the reinforcing metal structure and quickly render the
article unreliable.
[0007] As regards corrosion, the problem is particularly felt in tires. In fact, it frequently
occurs, especially in tires of heavy vehicles used on rough and stony ground, that
the tread is cut even deeply thus exposing the reinforcing metal structure to contact
with water and dampness. This promotes the start of reactions that corrode the metal
structure all the more quickly the less compact and uniform is the brass coating and
they propagate throughout the reinforcing metal structure rendering the tire unsuitable
for use.
[0008] The known processes for coating a metal element with a layer of brass can be divided
into two families: codeposition and diffusion.
[0009] The codeposition processes are characterized by the electrolytic codeposition of
copper and zinc.
[0010] The conventional process of codeposition that gives the best results, in terms of
compactness, uniformity and homogeneousness of the deposited layer of brass, is that
which involves the use of alkali cyanide baths containing a complex cyanide of bivalent
copper, a complex cyanide of zinc, free cyanide, and other compounds acting as brighteners,
such as carbonates, ammonia, etc.. This process is known as "cyanide process".
[0011] It is, however, well known that cyanides imply serious problems of toxicity for the
operators and their disposal involves costly and not altogether satisfactory techniques.
[0012] In order to overcome these drawbacks, many electrolytic baths have been evaluated
having various compositions. For examples, sulfates, tartrates, oxalates, pyrophosphates
and ethylenediamine, or even mixed systems such as chlorides/oxalates. However, the
results achievable with the cyanide process have not yet been attained.
[0013] It has also been proposed to add histidine to a pyrophosphate bath. This system has
given satisfactory results when carried out with a low density of cathode current
and at 30°C. However, when the density of cathode current exceeds 3 A/dm
2, the deposit has a powdery appearance and a burnt colour (Y. Fujiwara and H. Enomoto
"Composition, Structure and Morphology of Cu-Zn Alloy Deposits from Pyrophosphate
Baths", Plate and Surface Finishing, January 1993, pages 52-56).
[0014] A second way by which attempts have been made to replace the cyanide process are
that of the diffusion processes. These methods comprise the electrodeposition of one
or two layers of copper on steel, followed by the electrodeposition of a layer of
zinc and by a heat treatment whose purpose is to diffuse zinc in the layers of copper,
thus forming a layer of brass.
[0015] However, even the processes of this family have several drawbacks.
[0016] A first drawback is that each electrodeposition step requires its own tank and this
involves a costly and bulky plant.
[0017] A second drawback is that this process requires a careful selection and control of
several parameters in a plurality of tanks.
[0018] A third drawback is the cost of the energy required in the heat treatment that causes
the diffusion.
[0019] A fourth drawback is that the heat treatment causes some worsenings in the mechanical
properties of steel; in particular the ultimate tensile strength shows a reduction
of some 5 percent.
[0020] A further drawback of these processes is that the heat treatment causes the formation
of some quantities of zinc oxide.
[0021] In order to overcome these drawbacks, it is a first object of the present invention
to provide a process of electrolytic codeposition of copper and zinc on a metal element
wherein said process, while not using any cyanide, gives results at least equal to
those of the cyanide process.
[0022] A second object of the present invention is to provide a metal element coated with
a brass layer that, while not having been deposited with the cyanide process, has
properties at least equal to those of a similar metal element that has been coated
with brass according to the cyanide process.
[0023] A third object of the present invention is to provide an article of manufacture comprising
a reinforcing metal element embedded in a vulcanized elastomeric matrix wherein said
reinforcing element consists of at least a steel wire coated with a layer of brass
that, while not having been deposited with the cyanide process, has properties at
least equal to those of a similar wire that has been coated with brass according to
the cyanide process.
[0024] These and other objects have been achieved with the process of the present invention
that is based on the finding that an electrolytic bath similar to that described by
Y. Fujiwara and H. Enomoto gives altogether unexpected results when carried out at
temperatures of from 40°C to 55°C. In fact, when working at these temperatures, excellent
brass coatings are obtained even with a density of cathode current equal to or greater
than 25 A/dm
2 and this means a productivity equal to at least 8 times that of the process of Y.
Fujiwara and H. Enomoto.
[0025] Unless otherwise specified , in the present description and in the claims, the expression
"metal element" means any metal article that can be coated with a layer of brass by
an electrolytic method such as, for example, articles for bathroom, sanitary and electrical
use, door and window frames and articles for personal use. Specific examples of such
articles are: taps, handles, small metal items, chandeliers, spectacle frames and
the like. Preferably, the metal element consists of iron and alloys thereof, aluminium
and zinc. Even more preferably, the metal element consists of a steel wire having
a carbon content of from 0.6 to 0.95%. Typically, said steel wire is suitable for
being corded into cords and forming internal reinforcing structures for articles made
of vulcanized elastomeric material such as tires, conveyor belts, transmission belts
and flexible pipes of natural or synthetic rubber or mixtures thereof.
[0026] The term "brass" means a metal composition, as homogeneous as possible, consisting
of from 10% to 50% by weight of zinc and from 90% to 50% by weight of copper, preferably
from 20% to 40% by weight of zinc and from 80% to 60% by weight of copper and, even
more preferably, from 30% to 40% by weight of zinc and from 70% to 60% by weight of
copper.
[0027] The term "cord" means a cord obtained by cording, according to conventional techniques,
of steel wires coated with a layer of brass that, before drawing, is from 1 to 3 microns
thick while, after drawing, it is from 0.1 to 0.4 microns thick. Generally, the diameter
of said wires is about 1-3 mm before drawing and 0.1-0.5 mm after drawing. Typically,
a cord commonly used in reinforcing structures of giant radial tires consists of 7
strands, each of 4 wires with a diameter of about 0.175 mm, round which a wire is
wound, known as wrapper, having a diameter of 0.15 mm.
[0028] The expression "cathodic efficiency" means the percent ratio between the amount of
metal actually deposited and the theoretical amount of metal that should have been
deposited according to the Faraday's rule.
[0029] The present invention relates to a process of electrolytic codeposition of copper
and zinc on a metal element wherein the electrolytic bath consists of an aqueous solution
of at least a bivalent copper salt, at least a zinc salt and an alkali pyrophosphate,
characterized in that
- said bath also comprises an amino acid compound of formula

wherein Y is O, S or NR3,
R1, R2 and R3, the same, or different, are hydrogen or a lower alkyl, or an acid-addition salt
thereof, and that
- the bath temperature is of from 40°C to 55°C.
[0030] A preferred meaning of Y is NR
3.
[0031] Preferred meanings of R
1, R
2 and R
3, are hydrogen, methyl and ethyl.
[0032] Preferably, the amino acid compound of formula (I) is histidine hydrochloride.
[0033] As opposed to brass deposits obtained by means of diffusion, the deposit of brass
obtained with the process of the present invention is characterized by a substantially
constant content of copper and of zinc throughout the depth of the deposit.
[0034] Hence, it is a second object of the present invention to provide a metal element
coated with a layer of brass having a substantially constant content of copper and
of zinc throughout the deposit wherein said layer has been deposited according to
the process of the present invention.
[0035] Moreover, it is a third object of the present invention to provide an article of
manufacture comprising a reinforcing metal element embedded in a vulcanized elastomeric
matrix wherein said reinforcing element consists of at least a steel wire coated with
a layer of brass, characterized in that said layer has been deposited according to
the process of the present invention.
[0036] Preferably, said article of manufacture is a vehicle tire, a transmission belt, a
belt for a conveyor or a pipe.
[0037] Fig. 1 is a diagram showing the amount of copper deposited depending on the density
of the cathode current applied when using a galvanic bath of the present invention
that had the following characteristics:
Cu
++ = 0.2M, Zn
++ = 0.12M, histidine = 0.01 M, T = 45°C.
[0038] Fig. 2 is a diagram showing the cathode efficiency depending on the density of the
cathode current applied when using a galvanic bath of the present invention that had
the following characteristics:
Cu
++ = 0.2M, Zn
++ = 0.12M, histidine = 0.01 M, T = 45°C.
[0039] Fig. 3 is a diagram showing the amount of copper deposited depending on the Cu
++/Zn
++ mole ratio present in a galvanic bath of the present invention run under the following
conditions:
pH = 9, T = 45°C, i = 24 A/dm
2.
[0040] Fig. 4 shows a cord made of metal wires of the present invention embedded in a vulcanized
elastomeric matrix.
[0041] Fig. 5 shows a cross-sectional view of a tire reinforced with cords made of metal
wires of the present invention.
[0042] Fig. 6 shows a cross-sectional perspective view of a conveyor belt reinforced with
cords made of metal wires of the present invention.
[0043] Fig. 7 shows a cross-sectional perspective view of a transmission belt reinforced
with cords made of metal wires of the present invention.
[0044] Fig. 8 shows a cross-sectional perspective view of a flexible pipe reinforced with
cords made of metal wires of the present invention.
[0045] Before being dipped in the galvanic bath to be coated with a layer of brass according
to the process of electrolytic codeposition of the present invention, the metal element
is pickled according to conventional techniques, to remove any possible surface layer
of oxides.
[0046] Preferably, the galvanic bath of the present invention is characterized by:
A) a content of Cu++ of from 0.1 to 0.35 moles/litre;
B) a Cu++/Zn++ mole ratio of from 0.9 to 9;
C) a (Cu++)+(Zn++)/alkali pyrophosphate mole ratio of from 0.13 to 0.45;
D) a (Cu++)+(Zn++)/amino acid compound mole ratio of from 13 to 45.
[0047] Examples of suitable copper salts are hydrate or anhydrous cupric sulfate.
[0048] Examples of suitable zinc salts are hydrate or anhydrous zinc sulfate.
[0049] Typical examples of an alkali pyrophosphate are sodium and potassium pyrophosphate.
[0050] A typical example of an amino acid compound is histidine, preferably in the form
of an acid addition salt such as, for example, hydrochloride.
[0051] Typically the density of cathodic current is of from 2 to 40 A/dm
2. Preferably, it is of from 10 to 40 A/dm
2, even more preferably it is of from 20 to 30 A/dm
2.
[0052] According to a preferred embodiment of the present invention, a galvanic bath for
depositing a brass layer comprising from 60% to 70% of copper and from 40% to 30%
of zinc has the following composition:
|
mols/litre |
Cu++ |
0.18 - 0.26 |
Zn++ |
0.087 - 0.14 |
alkali pyrophosphate |
0.9 - 1.09 |
amino acid compound |
0.09 - 0.011 |
[0053] Suitable materials to prepare the abovementioned bath are:
|
grams/litre |
cupric sulfate pentahydrate |
45 - 65 |
zinc sulfate heptahydrate |
25 - 40 |
potassium pyrophosphate |
300 - 360 |
histidine monohydrochloride |
1.8 - 2.2 |
Bath temperature |
40 - 55°C; preferably 45°C. |
Bath pH |
8.5 - 9.7; preferably 8.8 - 9. |
Density of cathode current |
10 - 40 A/dm2. |
[0054] Both soluble anodes and insoluble anodes may be used.
[0055] In the first case brass anodes are used, having the same copper percent as that desired
in the deposit.
[0056] Example of a suitable material for insoluble anodes is titanium, possibly coated
with oxides of suitable materials such as iridium and tantalum.
[0057] The anodes may be placed parallel to the wire or on the bottom of the cups.
[0058] After electrodeposition of a brass layer, the metal element is preferably treated
on its surface with a phosphating bath consisting of a 30 - 50 g/l solution of phosphoric
acid at a temperature of 30°C - 50°C, for an immersion time of from 3 to 5 seconds.
[0059] When the metal element is a steel wire coated with a layer of brass (1 - 2 microns),
it is preferably drawn using a conventional emulsion lubricant.
[0060] The wire can then be used to produce cord of the type shown in Fig. 4.
[0061] As shown in the diagram of Fig. 1, a further advantage of the present invention is
that the density of the cathode current does not have a significant effect on the
percent of deposited copper. The distribution of the current itself (depending on
different cell forms, different bath stirring, and the like) also has no significant
effect on the percent of deposited copper.
[0062] As shown in Fig. 2, the cathode efficiency of the process of the present invention
is about 70% while, in the case of the cyanide bath it is, for the same cathode current,
substantially less.
[0063] As shown in Fig. 3, the amount of copper deposited with the process of the present
invention is a linear function of the copper/zinc ratio.
[0064] This further advantage of the present invention allows the composition of the bath
to be preselected very easily in accordance with the brass composition that it is
desired to deposit.
[0065] Fig. 5 shows a tire produced in a known way but using cords made of steel wires coated
with brass deposited according to the present invention. The tire is fitted on a rim
13 and consists of a bead 10, a bead ring 12, a carcass ply 14, belt strips 15, tread
16 and sidewalls 17. The strips 15 are formed by cords of steel wire coated with brass
with the process of the present invention.
[0066] Figs. 6-8 show a conveyor belt 20, a transmission belt 30 and a flexible pipe 40
made of vulcanized natural or synthetic rubber, respectively, each reinforced with
cords made of steel wire coated with brass according to the process of the present
invention.
[0067] The following examples are intended to further illustrate the present invention without,
however, limiting it in any way.
EXAMPLE 1
[0068] A galvanic bath capable of depositing a layer of brass consisting of about 90% of
copper and about 10% of zinc on a steel wire has the following composition:
|
mols/litre |
Cu++ |
0.15 |
Zn++ |
0.06 |
alkali pyrophosphate |
1 |
histidine |
0.01 |
[0069] The materials used to prepare the abovementioned bath were:
|
grams/litre |
cupric sulfate pentahydrate |
37 |
zinc sulfate heptahydrate |
17 |
potassium pyrophosphate |
330 |
histidine monohydrochloride |
2 |
[0070] Working conditions:
Bath temperature |
45°C |
Bath pH |
9 |
Density of cathode current |
2 A/dm2. |
EXAMPLE 2
[0071] A galvanic bath capable of depositing a layer of brass consisting of about 80% of
copper and about 20% of zinc on a steel wire has the following composition:
|
mols/litre |
Cu++ |
0.1 |
Zn++ |
0.05 |
alkali pyrophosphate |
1 |
histidine |
0.01 |
[0072] The materials used to prepare the abovementioned bath were:
|
grams/litre |
cupric sulfate pentahydrate |
25 |
zinc sulfate heptahydrate |
14 |
potassium pyrophosphate |
330 |
histidine monohydrochloride |
2 |
[0073] Working conditions:
Bath temperature |
45°C |
Bath pH |
9 |
Density of cathode current |
5 A/dm2. |
EXAMPLE 3
[0074] A galvanic bath capable of depositing a layer of brass consisting of about 67% of
copper and about 33% of zinc on a steel wire has the following composition:
|
mols/litre |
Cu++ |
0.24 |
Zn++ |
0.13 |
alkali pyrophosphate |
1 |
histidine |
0.01 |
[0075] The materials used to prepare the abovementioned bath were:
|
grams/litre |
cupric sulfate pentahydrate |
60 |
zinc sulfate heptahydrate |
38 |
potassium pyrophosphate |
330 |
histidine monohydrochloride |
2 |
[0076] Working conditions:
Bath temperature |
45°C |
Bath pH |
9 |
Density of cathode current |
25 A/dm2. |
EXAMPLE 4
[0077] A galvanic bath capable of depositing a layer of brass consisting of about 64% of
copper and about 36% of zinc on a steel wire has the following composition:
|
mols/litre |
Cu++ |
0.2 |
Zn++ |
0.118 |
alkali pyrophosphate |
1 |
histidine |
0.01 |
[0078] The materials used to prepare the abovementioned bath were:
|
grams/litre |
cupric sulfate pentahydrate |
50 |
zinc sulfate heptahydrate |
34 |
potassium pyrophosphate |
330 |
histidine monohydrochloride |
2 |
[0079] Working conditions are:
Bath temperature |
45°C |
Bath pH |
9 |
Density of cathode current |
25 A/dm2. |
EXAMPLE 5
[0080] A galvanic bath capable of depositing a layer of brass consisting of about 60% of
copper and about 40% of zinc on a steel wire has the following composition:
|
mols/litre |
Cu++ |
0.1 |
Zn++ |
0.07 |
alkali pyrophosphate |
1 |
histidine |
0.01 |
[0081] The materials used to prepare the abovementioned bath were:
|
grams/litre |
cupric sulfate pentahydrate |
25 |
zinc sulfate heptahydrate |
20 |
potassium pyrophosphate |
330 |
histidine monohydrochloride |
2 |
[0082] Working conditions:
Bath temperature |
45°C |
Bath pH |
9 |
Density of cathode current |
16 A/dm2. |
EXAMPLE 6
[0083] A galvanic bath capable of depositing a layer of brass consisting of about 50% of
copper and about 50% of zinc on a steel wire has the following composition:
|
mols/litre |
Cu++ |
0.1 |
Zn++ |
0.1 |
alkali pyrophosphate |
1 |
histidine |
0.01 |
[0084] The materials used to prepare the abovementioned bath were:
|
grams/litre |
cupric sulfate pentahydrate |
25 |
zinc sulfate heptahydrate |
29 |
potassium pyrophosphate |
330 |
histidine monohydrochloride |
2 |
[0085] Working conditions:
Bath temperature |
45°C |
Bath pH |
9 |
Density of cathode current |
16 A/dm2. |
[0086] Similar results have been obtained by working under conditions similar to those described
in the preceding Examples from 1 to 6 both at 40°C and at 50°C but the appearance
of the layer of brass deposited was slightly less uniform than that deposited at 45°C.
TESTS
[0087] The morphological and structural properties of brass deposits obtained according
to Examples from 1 to 6 have been evaluated both under an electron microscope with
a magnification of 2,500 and Auger spectroscopy.
[0088] Examination under the electron microscope has shown that the deposits richest in
zinc (i.e. copper< 60%) exhibit a substantially smooth surface while the poorest ones
(i.e. copper ≧ 60%) exhibit a compact surface with a semispheroidal morphology having
a size of from about 0.5 to 1 microns.
[0089] This morphological feature sharply distinguishes the brass deposits of to the present
invention over those obtained by diffusion which, before drawing, show a highly irregular
surface with holes of a size of from 0.1 to 0.5 microns.
[0090] Further differences have been detected by means of the Auger spectroscopy.
[0091] In fact the brass deposits according to the present invention are characterized by
a substantially constant content of copper and zinc throughout the depth of the deposit
while those obtained by diffusion show, before the drawing step, deviations of some
10%, as gradient of diffusion (diffusion % of Cu between the outside and the inside).
[0092] Moreover, the surfaces of the brass deposits obtained by diffusion show, before the
drawing step, some amounts of oxides, particularly of zinc, evaluated by detecting
the content of oxygen, [estimated as the ratio O/(Cu+Zn)], which is of from about
5% to about 10%. In contrast, the surface of deposits obtained according to the present
invention have a content of oxygen equal to or less than about 3%.
1. A process for electrolytic codeposition of copper and zinc on a metal element wherein
the electrolytic bath consists of an aqueous solution of at least a salt of bivalent
copper, at least a salt of zinc and an alkali pyrophosphate, characterized in that
- said bath also comprises an amino acid compound of formula

where Y is O, S or NR3,
R1, R2 and R3, the same, or different, are hydrogen or lower alkyl, or an acid-addition salt thereof,
and that
- the bath temperature is of from 40°C to 55°C.
2. A process according to claim 1, characterized in that Y is NR3.
3. A process according to claim 1 or 2, characterized in that R1 is hydrogen, methyl or ethyl.
4. A process according to any claim from 1 to 3, characterized in that R2 is hydrogen, methyl or ethyl.
5. A process according to any one of the claim from 1 to 4, characterized in that R3 is hydrogen, methyl or ethyl.
6. A process according to any claim from 1 to 5, characterized in that the amino acid
compound of formula (I) is histidine hydrochloride.
7. A process according to any claim from 1 to 6, characterized in that the density of
the cathode current is of from 2 A/dm2 to 40 A/dm2.
8. A process according to any claim from 1 to 6, characterized in that the density of
the cathode current is of from 10 A/dm2 to 40 A/dm2.
9. A process according to any claim from 1 to 6, characterized in that the density of
the cathode current is of from 20 A/dm2 to 30 A/dm2.
10. A metal element coated with a layer of brass having a substantially constant content
of copper and of zinc throughout the deposit, characterized in that said layer has
been deposited according to the process of any one of the preceding claims from 1
to 9.
11. An article of manufacture comprising a reinforcing metal element embedded in a vulcanized
elastomeric matrix wherein said reinforcing element consists of at least a steel wire
coated with a layer of brass, characterized in that said layer has been deposited
according to the process of any one of the preceding claims from 1 to 9.
12. An article of manufacture according to claim 11, characterized in that it is a tire
for a vehicle, a transmission belt, a conveyor belt or a pipe.