[0001] The present invention relates to new bath permitting, by chromium plating, to obtain
a shiny black coating on surfaces of zinc, or zinc-or cadmium-containing alloys.
[0002] The protection of surfaces of zinc, or of zinc-or cadmium-containing surfaces by
chromium-plating said surfaces, has already been described.
[0003] The solutions used to this effect contain essentially chromium (for example in sodium
or potassium dichromate and or chromic acid form), sulphate ions and, in some cases
a metallic compound giving rise to the formation of a suitably coloured chromate deposit.
[0004] Amongst the metallic compounds that can be used, there are the silver salts (for
example silver nitrate) which lead to the formation of a shiny black chromium plating
film, which looks good but of which the resistance to corrosion is affected by metallic
pollutions (zinc, iron, etc.).
[0005] However, the baths usable for obtaining these silver-containing coatings are rather
expensive to prepare and to maintain. For this reason, attempts have been made to
find compounds of metals other than silver which, when used in chromium-plating baths,
could give black, shiny and corrosion-resistant coatings.
[0006] A chromium-plating bath has recently been described which contains besides chromium
(6) and sulphate ions, a copper salt and a mixture of acetic acid and formic acid.
Unfortunately, when using this kind of bath, the deposit obtained is dull, this making
it less interesting at the industrial level.
[0007] It is the object of the present invention to overcome this drawback by proposing
a method for chromium-plating surfaces of zinc, or of zinc or cadmium alloys, the
said method producing a shiny black coating with good adherence to the support and
ensuring a good protection against corrosion of the support, which method consists
in placing the support to be chromium - plated in contact with a bath containing:
5 - 40 g/l , expressed in Cr, of hexavalent chromium,
sulphate ions,
0.025 - 40 g/l of cupric ions,
0.1 - 5 g/l of ions selected from silver and the molybdic ion,
30 - 120 g/l of acetic acid,
and 0 - 6 g/l of formic acid.
[0008] The invention further relates to the baths used in carrying out the said method.
[0009] It will be noted:
- that the quantities of chromium ions to be used are substantially the same as those
currently used in the chromium-plating baths,
that sulphate ions are used, as known,. the effect of these ions being, all other
things being equal, to improve the plating speed and also the adherence of the deposits
to the support, especially when said sulphate ions are added in the form of sodium
sulphate and sulphuric acid; said sulphate ions can also be added in the form of a
copper sulphate for example,
- and that cupric ions will be used in any case, these ions producing a chromium-plating
of a very pleasant colour,
- that the shiny finish of the deposits is obtained due to the presence, with the
cupric ions, of another ion selected from silver or the molybdic ion.
[0010] It is known that the use of silver has already been recommended, but the simultaneous
use of copper ions and silver ions has never been described. When simultaneously using
these two ions, the operation will take place, according to the invention, in the
presence of preferably 0.025 - 0.2 g/l of copper ions and preferably
0.1 - 0.2 g/l of silver ions. It is inside these ranges of concentration that the
best results are obtained.
[0011] The use of molybdic (

) ions with the copper ions, also produces according to the invention, a shiny black
deposit with excellent anti-corrosion properties. The simultaneous use of copper ions
and molybdic ions implies that fairly large quantities of these ions are used; the
best results are obtained when operating with concentrations of between 15 and 30
g/l of copper ions and between 0.15 and 5 g/l of molybdic ions (

);
- that in all cases (whether using the copper-silver combination, or the copper-molybdate
combination or the copper-silver-molybdate combination) the baths will contain acetic
acid; the concentrations of that acid are variable and can be between about 30 and
about 120 g/l. Advantageously, they will be between 65 and 90 g/l,
- that, finally, in the special case of a copper-molybdate bath, it is advantageous
to use, in addition to acetic acid, a certain quantity of formic acid, the preferred
concentration of this acid being about 3 g/1.
[0012] The conditions of operation, to obtain the chromium-plating according to the invention
can be the conditions conventionally used for chromium-plating zinc or cadmium surfaces.
These conditions are for example:
- a pH obviously acid, between 0.5 and 4,
- a temperature approaching the ambient temperature, i.e. between about 15 and 40°C,
- a period of contact of the piece to be treated and the bath, which can vary, depending
on the Deaths, between 10 seconds and 10 minutes,
- with or without stirring.
[0013] The pieces to be treated according to the invention have of course a coating of black
and shiny chromate which is very adherent and constitutes a good protection against
corrosion.
[0014] It is however possible to further improve the properties of these coatings, and in
particular in certain cases, the shiny finish of the deposit, and its efficiency as
a protector against corrosion, by submitting the piece thus coated to a post-rinse
with a phosphating bath. The usable phosphating baths are known per se and have already
been recommended for certain applications, such as for example for polishing certain
deposits. It is considered that in the case of the deposits according to the invention
(copper-silver or copper-molybdates) such rinsing baths are specifically efficient
and especially advantageous in that they improve the protective effect of the coatings.
Amongst the baths usable, the following are given by way of example and non-restrictively:
- baths containing up to 5% by weight of phosphoric acid,
- baths'containing between 5 and 20 g/l of sodium hexametaphosphate,
- baths containing between 0.5 and 15 g/l of monosodium phosphate and between 0.5
and 15 g/l of monopotassium phosphate.
[0015] As indicated hereinabove, the exact composition of phosphating baths can vary to
large extents, but very good results have always been obtained with the special baths
indicated hereinabove.
[0016] The conditions required for this phosphating treatment are usually as follows:
- ambient temperature, i.e. between 15 and 40°C,
- duration between 10 seconds and 5 minutes, in general about one minute.
- with or without stirring.
[0017] The following examples are given by way of information and non-restrictively.
Example 1
[0018] To protect a steel coated with a layer of zinc.
[0019] A bath was prepared for this purpose containing:

[0020] The piece to be protected was dipped into this bath, at ambient temperature (20-27°C)
with air-stirring of the bath, and for a duration of 2 minutes.
[0021] The resulting shiny black piece was then rinsed and dipped into a phosphating bath
containing 12 g/l of sodium hexametaphosphate, for one minute at 20°C, without stirring.
[0022] The piece removed from the bath was then dried.
Example 2
[0023] A bath was prepared containing:

[0024] The piece to be treated was dipped in this bath (at 20°C) for about 2 minutes. The
resulting piece, once removed from the bath and after rinsing, can be given the phosphating
treatment to improve the polished finish and resistance to corrosion of the protective
coating.
1. An aqueous bath for producing a black chromate plating of a zinc surface or of
a surface of a zinc alloy or a cadmium alloy characterized by a content of:
(i) sulphate ions;
(ii) 5 to 40 g/l of hexavalent chromium;
(iii) 0.025 to 30 g/l of copper ions;
(iv) 0.1 to 5 g/1 of silver ions and/or molybdic (

) ions;
(v) 30 to 120 g/1 of acetic acid;
(vi) 0 to 6 g/l of formic acid.
2. An aqueous bath according to Claim 1, wherein the amount of copper ions is 0.025
to 0.2 g/l and the amount of silver ions is 0.1 to 0.2 g/1.
3. An aqueous bath according to Claim 1, wherein the content of copper ions is 15
to 30 g/l and the content of molybdic ions is 0.15 to 5 g/l.
4. An aqueous bath according to Claim 3, containing formic acid in a quantity of about
3 g/l.
5. A method for producing a black chromate plating of a zinc surface or of a surface
of a zinc alloy or a cadmium alloy characterized in that an article with a surface
of zinc, zinc alloy or cadmium alloy to be chromium plated is dipped in an aqueous
bath as defined in any one of Claims 1 to 4 for sufficient time to produce a black
chromate layer of the required thickness.
6. A method according to Claim 5, wherein the bath is at a temperature of 15° to 40°C.
7. A method according to Claim 5 or Claim 6 wherein the time of immersion is 10 seconds
to 10 minutes.
8. A method according to any one of Claims 5 to 7, wherein the bath is at a pH of
between 0.5 and 4.
9. A method according to any one of Claims 5 to 8, wherein the thus plated article
is rinsed and then dipped into a phosphating bath.