[0001] The present invention relates to a continuous chemical patination/satinising treatment
process for zinc-titanium alloys used in the construction industry, in particular
for roofs, facades, guttering, interiors or architectural works.
Prior art
[0002] Zinc-titanium alloy laminates are widely used in the construction industry, especially
for roofing and cladding. The natural appearance of these claddings can be varied
by particular pre-patination surface treatments.
[0003] Said processes must give coil surfaces having a chemical composition complying with
Standard EN 988 - 1998 (see Table 1) an attractive appearance with a patinated effect,
specific colouring, such as antique-look zinc, excellent antifinger properties, and
high corrosion resistance.
Table 1
Element |
Standard EN 988 - 1998 |
Al |
< 0.0150% |
Cu |
0.0800 - 1.0000% |
Pb |
< 0.0030% |
Cd |
< 0.0030% |
Fe |
< 0.0020% |
Sn |
< 0.0010% |
Ti |
0.0600 - 0.2000% |
[0004] The known process normally comprises the following stages:
- degreasing with an alkaline grease-removal liquid in aqueous solution
- first rinse with continuously fresh water
- acid treatment involving chemical patination/satinising with specific products
- second rinse with continuously fresh water
- final passivation treatment
- drying of wet film.
[0005] EP 827785 describes a process for the treatment of zinc-titanium laminates characterised by
the use of a pickling bath based on nitric and sulphuric acid and a passivation stage
with a polymer containing chromate.
Disclosure of the invention
[0006] An improved process has now been found which is characterised, after the second rinse
with water, by a pre-passivation stage followed by drying with hot air to prevent
the formation of surface zinc oxides, and the use of a polyacrylic resin as antifinger
agent in the final passivation treatment.
[0007] The process of the invention comprises the following stages in particular:
[0008] Degreasing serves to eliminate all trace of oils, fats, cleaning paste, oxides and
any other impurities from the coil surface, in order to have a perfectly clean metal
surface ready for subsequent treatments.
[0009] Normally, said degreasing is performed with liquid products in aqueous solution at
an alkaline pH (10-14). The use concentration is between 1% and 10%, and the temperature
of the working bath between 50°C and 70°C, for a treatment time of between 5 and 40
seconds, with spray pressures of between 1 and 4 bars. The main elements of the degreasing
bath are listed in Table 2 below.
Table 2
Element |
Concentration |
KOH or NaOH |
2 - 20 g/l |
P2O5 |
2 - 20 g/l |
Surfactants |
200 - 3000 ppm |
Sequestering additives |
1 - 10 g/l |
[0010] P
2O
5 is present either as orthophosphates (monosodium, disodium or trisodium phosphate)
or as polyphosphates (tripolyphosphate or neutral pyrophosphate), all in the form
of sodium or potassium salts.
[0011] The most commonly used surfactants are ethoxylated fatty alcohols with alcohol C9-C11
chain, C12-C13 or C12-C18, having different degrees of ethoxylation or containing
different numbers of ethylene oxide moles.
[0012] The sequestering additives are organic compounds selected from nitriloacetic acid,
sodium gluconate, gluconic acid, ethylenediaminetetraacetic acid disodium, ethylenediaminetetraacetic
acid trisodium, phosphonates, acrylates and polyacrylates.
[0013] The first rinse with continuously fresh water serves to eliminate all trace of the
preceding stage; the temperature is normally between 30°C and 60°C, with times ranging
between 5 and 30 seconds, and spray application.
[0014] The chemical patination/satinising treatment is performed by pickling the zinc-titanium
alloy with a surface attack between 5 and 20 g/m
2.
[0015] The treatment is usually performed with a specific product at a pH of between 0 and
2, used at concentrations of between 10 and 15%. The temperature of the working bath
can be between 50% and 70%, for a reaction time of between 10 and 30 seconds; the
spray pressures must be between 1 and 4 bars.
[0016] The main elements of the patination/satinising bath are listed in Table 3 below.
Table 3
Element |
Concentration |
H2SO4 |
10-150 g/l |
Surfactants |
1 - 15 g/l |
Process accelerant as NO3 |
100 - 6000 ppm |
Sequestering agents |
1 -100 g/l |
Elements deriving from pickling of the alloy |
Zn |
< 100 g/l |
Other metals originating from the alloy |
< 100 mg/l |
[0017] The process accelerator can consist of NO
3 donor compounds such as nitric acid, ammonium nitrate, nickel nitrate, sodium nitrate,
zinc nitrate, iron nitrate or cobalt nitrate, or nitrogenous organic compounds such
as nitroguanidine, used alone or mixed together. The surfactants and agents are the
same as already described.
[0018] The second rinse with continuously fresh water is performed as for the first rinse,
to eliminate all trace of the preceding stage; the temperature is normally between
30°C and 60°C, with times ranging between 5 and 30 seconds, and spray application.
[0019] Pre-passivation, which prevents the formation of zinc-oxides on the surface by increasing
the anti-corrosion properties of the coil, is performed by treatment with a chromium-free
bath containing zirconium and/or titanium and aluminium compounds.
[0020] The typical composition of a pre-passivation bath according to the invention is set
out in Table 4 below. The concentration of the product ranges between 1 and 5%, the
temperature between 30 and 60°C, and the treatment times between 1 and 10 seconds;
the product can be applied by spraying or immersion, and the pH value is < 5.
Table 4
Element |
Concentration |
Zr |
100 - 5000 mg/l |
Ti |
100 - 5000 mg/l |
Al |
10 - 500 mg/l |
NH3 |
100 - 1000 ppm |
[0021] The zirconium compounds are preferably selected from fluorozirconic acid, ammonium
zirconium carbonate and potassium fluozirconate; the aluminium compounds are selected
from aluminium oxide of various extractions (aluminas), aluminium fluoride and aluminium
bifluoride; the titanium compounds are selected from fluotitanic acid, titanium oxalate,
titanium oxide and potassium fluotitanate.
[0022] Drying is then performed with hot air from 50 to 90°C.
Final passivation treatment
[0023] The antifinger passivating product is applied with a Chem-Coater machine in two separate
application stages, with a wet film drying step between each stage.
[0024] The inorganic component is applied at the first stage. Depending on the process required,
the inorganic component can be one of three different types:
"Chromium 3 - Chromium 6 Version" (Version 1)
[0025] The product consists of chromic acid, chromium phosphate, corrosion inhibitors such
as zinc phosphate and zinc chromate, and reducing agents such as gluconic acid, citric
acid, saccharose, hydroxylamine, methanol, hydrogen peroxide and starch. The application
takes place continuously at a temperature of between 15°C and 40°C; the concentration
used depends on the wet film applied, which ranges between 2 and 10 ml/m
2; it is generally between 10 and 50%, so that the end result is a total chromium deposit
of 20 to 100 mg/m
2; its value is calculated from the mg of chromium, on the basis that 1 mg/m
2 of Cr = 16 mg/ m
2 of total coating.
[0026] An example of the composition of the bath is shown in Table 5 below.
Table 5
Element |
Concentration |
Total chromium (= chromium 3 + chromium 6) |
5 - 20% |
P2O5 |
1 - 5% |
Zinc |
2 - 8% |
"Chromium 3 Version" (Version 2)
[0027] The product consists of phosphoric acid, chromium phosphate, chromium nitrate, complexing
agents selected from salified phosphonates or acids, gluconic acid, citric acid, tartaric
acid, EDTA, glycolic acid and/or polyacrylates, corrosion inhibitors such as colloidal
silicon dioxides in suspension, possibly having different particle sizes, generally
below 30 µm, and with a SiO
2 content of between 10 and 50%, and finally, organic wetting agents based on alkoxypolypropoxypolyethoxy-ethyl-benzylether
or belonging to the perfluoroderivative family. The application takes place continuously
at a temperature of between 15°C and 40°C; the concentration used depends on the wet
film applied, which ranges between 2 and 10 ml/m
2; it is generally between 30 and 70%, so that the end result is a total chromium deposit
of 30 to 80 mg/m
2; its value is calculated from the mg of chromium, on the basis that 1 mg/m
2 of Cr = 32 mg/ m
2 of total coating.
[0028] An example of the composition of the bath is shown in Table 6 below.
Table 6
Element |
Concentration |
Total chromium (= chromium 3) |
20 - 200 g/l |
P2O5 |
10-150 g/l |
NO3 |
3 - 50 g/l |
SiO2 |
20 -200 g/l |
"Chromium-free - Chromium Version" (Version 3)
[0029] The product consists of silanes, selected from the families of 1-propylamine,3-(triethoxysilyl)-silane
and trimethoxy[3-(oxiranylmethoxy)-propyl]-silane, titanium salts deriving from fluotitanic
acid, titanium oxalate, titanium oxide or potassium fluorotitanate, alkaline phosphates
such as monobasic or dibasic ammonium phosphate, mono-, bi- or tribasic sodium phosphate,
acid or neutral potassium pyrophosphate, alkaline nitrates such as ammonium nitrate,
sodium nitrate or potassium nitrate, sequestering agents selected from nitriloacetic
acid, sodium gluconate, gluconic acid, ethylenediaminetetraacetic acid disodium, ethylenediaminetetraacetic
acid trisodium, phosphonates, acrylates and polyacrylates, and corrosion inhibitors
based on heavy metals such as vanadium, molybdenum, tungsten and cerium. The product
should be applied at room temperature, in concentrations ranging between 80 and 100%,
in such a way that the titanium deposit is between 4 and 8 mg/m
2 and the SiO
2 deposit between 70 and 140 mg/m
2; its value is calculated from the mg of titanium, on the basis that 1 mg/m
2 of Ti = 160 mg/m
2 of total coating.
[0030] An example of the composition of the bath is shown in Table 7 below.
Table 7
Element |
Concentration |
SiO2 |
10 - 150 g/l |
P2O5 |
10-150 g/l |
V |
≤ 100 ppm |
Ti |
≤ 200 ppm |
[0031] Drying is then performed with hot air from 50 to 90°C.
[0032] An antifinger agent is applied at the second stage, namely an aqueous solution of
corrosion inhibitors such as zinc oxide and P
2O
5 and an acrylic resin consisting of monomers based on butylacrylate, methylmethacrylate
and acrylic acid, having the following characteristics:
pH < 6; MW ≥ 250000; TG (glass transition temperature) between 30 and 45°C; dry residue
between 30 and 50%.
[0033] In the case of version 1 only, the antifinger passivation product can also be applied
in a single stage, with a Chem-Coater machine. Depending on the final chromium deposit
desired, the bath is prepared with 1 part inorganic to 2 parts organic component,
or 1 part inorganic to 3 parts organic component. The quantity of mixture applied
is 2 to 6 ml/m
2. There is a partial reduction of chromium from 6 to 3 during this stage.
[0034] The wet film is then dried at a belt temperature of 80 to 140°C.
Laboratory test procedures
Degreasing:
[0035]
Element |
Concentration |
KOH |
4 g/l |
P2O5 from neutral potassium pyrophosphate |
5 g/l |
Surfactants with C9-C11 chain + 5 and 6 moles of OE = ethylene oxide |
500 ppm |
Sodium gluconate |
3 g/l |
|
Use concentration of product |
3 - 5% |
Temperature |
50 - 60°C |
Treatment time |
10 sec. |
Spray pressure |
2 bars |
First rinse
[0036]
Continuously fresh water |
- |
Temperature |
30°C |
Treatment time |
10 sec. |
Spray pressure |
2 bars |
Chemical patination/satinising treatment:
[0037]
Element |
Concentration |
H2SO4 |
60 g/l |
HNO3 |
6 g/l |
Surfactants with C9-C11 chain + 5 and 6 moles of OE = ethylene oxide |
1500 ppm |
Sodium gluconate |
10 g/l |
|
Use concentration of product |
10% |
Temperature |
60 - 70°C |
Treatment time |
10 sec. |
Spray pressure |
2 bars |
Second rinse
[0038]
Continuously fresh water |
- |
Temperature |
30°C |
Treatment time |
10 sec. |
Spray pressure |
2 bars |
Pre-passivation
[0039]
Element |
Concentration |
Zr (from fluorozirconic acid) |
500 mg/l |
Ti (from fluotitanic acid) |
300 mg/l |
Al (from alumina) |
50 mg/l |
NH3 |
50 ppm |
|
Use concentration of product |
2 - 3% |
Temperature |
50°C |
Treatment time |
2 sec. |
pH |
4 |
[0040] Drying is typically performed with hot air at a temperature of between 60 and 80°C.
Final passivation
First stage: "Chromium 3 - Chromium 6 Version"
[0041]
Element |
Concentration |
Total chromium (= chromium 6 + chromium 3) |
13% |
P2O5 |
3% |
Zinc |
3% |
|
Reducing agent used |
starch |
Wet film applied |
1 - 4 ml/m2 |
Temperature |
room |
First stage: "Chromium 3 version"
[0042]
Element |
Concentration |
Total chromium (= chromium 3) |
40 g/l |
P2O5 |
20 g/l |
NO3 |
5 g/l |
SiO2 |
40 g/l |
|
Complexing agent used |
Citric acid |
Type of silica used |
Particle size 15 µm - dry 30% |
Type of wetting agent |
perfluoroderivative |
Wet film applied |
1 - 4 ml/m2 |
Temperature |
room |
First stage: "Chromium-free version"
[0043]
Element |
Concentration |
SiO2 (from 1-propylamine,3-(triethoxysilyl)-silane and/or trimethoxy[3-(oxiranylmethoxy)propyl]-silane |
100 g/l |
P2O5 (from monobasic ammonium phosphate) |
20 g/l |
V |
100 ppm |
Ti (from fluotitanic acid) |
200 ppm |
|
Complexing agent used |
phosphonate |
Nitrate used |
ammonium nitrate |
Type of inhibitor selected |
vanadium |
Temperature |
room |
[0044] Drying is typically performed with hot air at a temperature of between 60 and 80°C.
Second stage: all versions.
[0045]
Resin used |
Pure acrylic, new formulation, inhibited,
with dry residue = 30%, pH = 4, TG = 32°C |
Wet film applied |
3-6 ml/m2 |
Single-stage application: "Chromium 3 - Chromium 6 Version"
[0046]
Dose ratios |
Inorganic ingredient 1 part - |
Organic ingredient 2 parts |
|
Inorganic ingredient 1 part - |
Organic ingredient 3 parts |
Wet film applied |
3 - 4 ml/m2 |
Temperature |
room |
[0047] Drying can be performed with hot air at a temperature of between 100 and 120°C.
Examples
[0048] The laboratory tests were performed to compare the results obtained with (i) cycles
not including the pre-passivation stage (conventional cycle) and (ii) other cycles
which were identical to the preceding ones except that they included the pre-passivation
stage and subsequent drying.
[0049] Two-stage application of the final passivating product and single-stage application
were tested in the cycles relating to the "Chromium 3 - Chromium 6 version"; 1:2 and
1:3 dose ratios of the two components were tested in the latter case.
[0050] Both the above-mentioned silanes, subsequently marked α and β, were tested in the
cycles relating to the "chromium-free version", both separately and in combined.
[0051] Only the acrylic resin according to the invention was used in the organic component
of the final passivation stage in all the cycles.
[0052] For convenience, the way in which the various cycles tested were marked is shown
in Table 8 below.
Table 8
Code |
Pre-passivation |
Passivation version |
Passivation |
Component dose ratio |
Type of silane |
A 1 |
No |
1 |
Biphasic |
|
|
A 1.2 |
No |
1 |
Monophasic |
2 : 1 |
|
A 1.3 |
No |
1 |
Monophasic |
3 : 1 |
|
A 2 |
No |
2 |
Biphasic |
|
|
A 3.1 |
No |
3 |
Biphasic |
|
α |
A 3.2 |
No |
3 |
Biphasic |
|
β |
A 3.3 |
No |
3 |
Biphasic |
|
α + β |
B 1 |
Yes |
1 |
Biphasic |
|
|
B 1.2 |
Yes |
1 |
Monophasic |
2 : 1 |
|
B 1.3 |
Yes |
1 |
Monophasic |
3 : 1 |
|
B 2 |
Yes |
2 |
Biphasic |
|
|
B 3.1 |
Yes |
3 |
Biphasic |
|
α |
B 3.2 |
Yes |
3 |
Biphasic |
|
β |
B 3.3 |
Yes |
3 |
Biphasic |
|
α + β |
[0053] After application of the cycles, the zinc-titanium alloy panels treated were subjected
to corrosion-resistance tests in a salt spray (fog) chamber, in accordance with Standard
ASTM B 117, unprotected panels and panels with protected edges being checked for the
appearance of the first white oxides.
[0054] Table 9 shows the results obtained, expressed as hours of exposure before the appearance
of the first white oxidation phenomena.
Table 9
Code |
Hours of exposure |
Code |
Hours of exposure |
A 1 |
72 |
B 1 |
96 |
A 1.2 |
72 |
B 1.2 |
96 |
A 1.3 |
72 |
B 1.3 |
96 |
A 2 |
60 |
B 2 |
72 |
A 3.1 |
60 |
B 3.1 |
72 |
A 3.2 |
60 |
B 3.2 |
72 |
A 3.3 |
72 |
B.3.3 |
96 |
1. A process of continuous chemical patination/satinising treatment of zinc-titanium
alloys comprising the following stages:
- degreasing with alkaline grease-removal liquid in aqueous solution;
- first rinse with continuously fresh water;
- chemical acid patination/satinising treatment;
- second rinse with continuously fresh water;
- pre-passivation treatment with a chromium-free bath containing zirconium and/or
titanium and aluminium compounds;
- air drying;
- passivation treatment comprising a first stage of treatment with a conventional
inorganic component based on chromium 3 and/or 6 or chromium-free, and a second stage
of treatment with an antifinger agent consisting of an aqueous solution of an acrylic
resin consisting of monomers based on butylacrylate, methylmethacrylate and acrylic
acid, having the following characteristics:
pH < 6;
MW ≥ 250000;
TG (glass transition temperature) between 30 and 45°C;
dry residue between 30 and 50%;
possibly mixed with corrosion inhibitors such as zinc oxide and P205;
- drying of wet film.
2. A process as claimed in claim 1, wherein the zirconium and/or titanium and aluminium
compounds in the pre-passivation bath are selected from fluorozirconic acid, ammonium
zirconium carbonate and potassium fluorozirconate; aluminium oxide of various extractions
(aluminas), aluminium fluoride and aluminium difluoride; fluorotitanic acid, titanium
oxalate, titanium oxide and potassium fluorotitanate.
3. A process as claimed in claim 1 or 2, wherein the passivation comprises treatment
with a bath containing chromium 3 and chromium 6 compounds.
4. A process as claimed in claim 3, wherein the bath contains chromic acid, chromium
phosphate, zinc phosphate and zinc chromate and reducing agents.
5. A process as claimed in claim 1 or 2, wherein the passivation comprises treatment
with a bath containing chromium 3 compounds.
6. A process as claimed in claim 5, wherein the bath contains phosphoric acid, chromium
phosphate, chromium nitrate, complexing agents, corrosion inhibitors and organic wetting
agents based on alkoxypolypropoxypolyethoxy-ethyl-benzylether or belonging to the
class of perfluoroderivatives.
7. A process as claimed in claim 1 or 2, wherein the passivation comprises treatment
with a chromium-free bath.
8. A process as claimed in claim 7, wherein the bath contains silanes, selected from
the classes of 1-propylamine,3-(triethoxysilyl)-silane and trimethoxy[3-(oxiranylmethoxy)propyl]-silane,
titanium salts deriving from fluorotitanic acid, titanium oxalate, titanium oxide
or potassium fluorotitanate, alkaline phosphates, alkaline nitrates, sequestering
agents selected from nitriloacetic acid, sodium gluconate, gluconic acid, ethylenediaminetetraacetic
acid disodium, ethylenediaminetetraacetic acid trisodium, phosphonates, acrylates,
polyacrylates, and corrosion inhibitors based on heavy metals selected from vanadium,
molybdenum, tungsten and cerium.