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Patent 2018631 Summary

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(12) Patent: (11) CA 2018631
(54) English Title: PROCESS FOR A PASSIVATING POSTRINSING OF PHOSPHATE LAYERS
(54) French Title: POSTRINCAGE-PASSIVATION DE COUCHES DE PHOSPHATE
Status: Deemed expired
Bibliographic Data
(52) Canadian Patent Classification (CPC):
  • 148/17
(51) International Patent Classification (IPC):
  • C23C 22/34 (2006.01)
  • C23C 22/06 (2006.01)
  • C23C 22/78 (2006.01)
  • C23C 22/83 (2006.01)
(72) Inventors :
  • HAUFFE, DIETER (Germany)
  • KOLBERG, THOMAS (Germany)
  • MULLER, GERHARD (Germany)
  • GEHMECKER, HORST (Germany)
  • RAUSCH, WERNER (Germany)
(73) Owners :
  • CHEMETALL GMBH (Germany)
(71) Applicants :
  • METALLGESELLSCHAFT AKTIENGESELLSCHAFT (Germany)
(74) Agent: ROBIC
(74) Associate agent:
(45) Issued: 1999-05-11
(22) Filed Date: 1990-06-08
(41) Open to Public Inspection: 1991-01-28
Examination requested: 1990-09-26
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
P 39 24 984.0 Germany 1989-07-28

Abstracts

English Abstract




In a process for a passivating postrinsing of
phosphate layers on metals before the application of a paint
or adhesive, aqueous solutions are employed which have been
adjusted to a pH value of 3 to 5 and which contain an
aluminum fluorozirconate in which the Al:Zr:F mole ratio is
(0.15 to 0.65):1:(5 to 7), and in which solutions the total
concentration of Al + Zr + F is 0.1 to 2.0 g/l, preferably
0.2 to 0.8 g/l. the postrinsing solutions may additionally
contain at least one of the anions benzoate, caprylate,
ethyl hexoate, salicylate in a total concentration of 0.05
to 0.5 g/l and may preferably be adjusted to the required pH
value with cations of volatile bases, such as ammonium,
ethanolammonium and di- and triethanolammonium. The paint
is subsequently applied suitably by cathodic electrocoating
or powder coating or from a low-solvent high-solids paint.


French Abstract

Dans un procédé pour post-rinçage-passivation de couches de phosphate sur des métaux avant l'application d'une peinture ou d'un adhésif, on utilise des solutions aqueuses dont le pH a été ajusté à une valeur de 3 à 5, et qui renferment un fluorozirconate d'aluminium, dans lequel le rapport molaire Al:Zr:F est de (0,15 à 0,65):1:(5 à 7), et où la concentration totale de Al + Zr + F est de 0,1 à 2,0 g/l, et préférablement 0,2 à 0,8 g/l. De plus, les solutions de post-rinçage peuvent contenir au moins l'un des anions benzoate, caprylate, éthylhexoate, salicylate, à une concentration totale de 0,05 à 0,5 g/l, et seront préférablement ajustées au pH requis à l'aide de cations de bases volatiles, comme les cations ammonium, éthanolammonium ainsi que di- et triéthanolammonium. La peinture est ensuite appliquée par électrodéposition cathodique ou revêtement en poudre, ou encore à partir d'un produit pauvre en solvant mais riche en solides.

Claims

Note: Claims are shown in the official language in which they were submitted.



The embodiments of the invention in which an
exclusive property or privilege is claimed are defined as
follows:

1. A process for a passivating postrinsing of
phosphate layers on metal surfaces, with a chromium-free
aqueous solution before the application of a paint or adhesive,
characterized in that the phosphated metal surfaces are rinsed
with an aqueous solution which have been adjusted to a pH value
of 3 to 5 and which contain an aluminum fluorozirconate in
which the Al:Zr:F mole ratio is (0.15 to 0.67):1:(5 to 7), and
in which solution the total concentration of Al + Zr + F is 0.1
to 2.0 g/l.

2. A process according to claim 1, wherein the
metals are selected from the group consisting of steel,
galvanized steel, zinc alloy-plated steel and aluminum.

3. A process according to claim 1 or 2,
characterized in that the phosphated metal surfaces are rinsed with
aqueous solutions in which the total concentration of Al + Zr
+ F is 0.2 to 0.8 g/l.

4. A process according to claim 1 or 2,
characterized in that the phosphated metal surfaces are rinsed with
aqueous solutions which contain in addition anions of at least
one of benzoate, caprylate, ethylhexoate and salicylate in a
total concentration of 0.05 to 0.5 g/l.

5. A process according to claim 1, 2, 3 or 4,
characterized in that the phosphated metal surfaces are rinsed
with aqueous solutions which have been pH-adjusted with cations
of volatile bases.

6. A process according to claim 1, 2, 3 or 4,
characterized in that the passivating postrinsing is succeeded


by final rinsing with deionized water.

7. A process according to claim 1, 2, 3 or 4,
characterized in that a paint is applied by cathodic
electrocoating after the passivating postrinsing.

8. A process according to claim 1, 2, 3 or 4,
characterized in that a paint is applied by powder coating
after the passivating postrinsing.

9. A process according to claim 1, 2, 3 or 4,
characterized in that a low-solvent high-solids paint is
applied after the passivating postrinsing.

10. A process according to claim 1, 2, 3 or 4,
characterized in that a coating composition containing a water
based solvent is applied after the passivating postrinsing.

11. A process according to claim 3, characterized in
that the phosphated metal surfaces are rinsed with aqueous
solutions which contain in addition at least one of the anions
benzoate, caprylate, ethylhexoate, salicylate in a total
concentration of 0,05 to 0,5 g/l.

12. A process according to claim 11, characterized
in that the phosphated metal surfaces are rinsed with aqueous
solutions which have been pH-adjusted with cations of volatile
bases.

13. A process according to claim 12, wherein the
cations of volatile bases are selected from the group
consisting of ammonium, ethanolammonium, di- and
triethanolammonium.

14. A process according to claim 11, characterized
in that the passivating postrinsing is succeeded by final

11
rinsing with deionized water.

15. A process according to claim 11, characterized
in that a paint is applied by cathodic electro-coating after
the passivating postrinsing.

16. A process according to claim 11, characterized
in that a paint is applied by powder coating after the
passivating postrinsing.

17. A process according to claim 11, characterized
in that a low-solvent high-solids paint is applied after the
passivating postrinsing.

18. A process according to claim 11, characterized
in that a coating composition containing a water based solvent
is applied after the passivating postrinsing.

Description

Note: Descriptions are shown in the official language in which they were submitted.


CA 02018631 1999-01-1~




The present invention relates to a process for a
passivating postrinsing of phosphate layers on metals,
particularly steel, galvanized steel, zinc alloy-plated
steel and aluminum, with a chromium-free aqueous solution
before the application of a paint or adhesive.
Phosphating is industrially employed on a large
scale for the preparation of metal surfaces for a
subsequent application of paint. The phosphate layers thus
formed result, inter alia, in an improved adhesion of the
paint films on the metals, an increased resistance to
corrosion and an inhibition of subsurface corrosion which
might be initiated at damaged portions of the paint film.
The protective properties of the phosphate layers may
further be improved by a passivating postrinsing with an
aqueous fluid.
Desirable properties from the aspect of
application technology will result from a passivating
postrinsing with fluids which contain hexavalent and/or
trivalent chromium. But the toxicity of the trivalent and
particularly of the hexavalent chromium compounds is often
regarded as a disadvantage.
Whereas US-A-4376000 describes a chromium-free
postrinsing agent which contains polyvinylphenol, that
agent must be used in a comparatively high concentration so
that its use will result in an undesired pollution of the
sewage, particularly because a large amount of oxygen is
required for the decomposition.

CA 02018631 1999-01-1~



US-A-3695942 discloses the use of soluble
zirconium compounds for an aftertreatment of conversion
layers. In addition to zirconium, the postrinsing agents
contain cations consisting of alkali and ammonium. The
reference contains an explicit warning against the use of
alkaline earth metal cations. Said postrinsing agents,
which are used at a pH value from 3 to 8.5, do not result
in the same quality as the chromium-containing agents.
US-A-3895970 describes acid aqueous postrinsing
agents for treating phosphate layers. Said agents
containing simple or complex fluorides and chromium-
zirconium fluoride and zirconium fluoride are mentioned as
zirconium compounds. With the exception of chromium-
zirconium fluoride, the products mentioned in that patent
will meet only medium requirements and chromium-zirconium
fluoride has the above-mentioned disadvanta~e that it is
toxic.
It is an object of the invention to provide for
the passivating postrinsing of phosphate layers on metals
before an application of a paint or adhesive a process
which is free of the disadvantages of the known processes
and distinguishes by providing a high protection against
corrosion and a strong adhesion to paint and adhesive and
does not pollute or only very slightly pollutes the
environment.
That object is accomplished in that a process of
the kind described first hereinbefore is carried out in
accordance with the invention in such a manner that the
phosphated metal surfaces are rinsed with aqueous solutions
which have been adjusted to a pH value of 3 to 5 and which
contain an aluminum fluorozirconate in which the Al:Zr:F

CA 02018631 1999-01-1~
.




mole ratio is (0.15 to 0.67):1:(5 to 7), and in which
solutions the total concentration of Al + Zr + F is 0.1 to
2.0 g/l.
According to a preferred feature of the invention
the phosphated metal surfaces are rinsed with aqueous
solutions in which the total concentration of Al + Zr + F
is 0.2 to 0.8 g/l.
The process in accordance with the invention is
suitable for treating phosphate layers of all types which
can be formed on metals, particularly on steel, galvanized
steel, steel plated with a zinc alloy, aluminum-plated
steel, zinc, zinc alloys, aluminum and aluminum alloys.
Such phosphates include, inter alia, zinc phosphate, iron
phosphate, manganese phosphate, calcium phosphate,
magnesium phosphate, nickel phosphate, cobalt phosphate,
zinc-iron phosphate, zinc-manganese phosphate, zinc-calcium
phosphate, and layers of other types, which contain two or
more divalent cations. The process is particularly suitable
for treating those phosphate layers which have been formed
by low-zinc phosphating processes with or without an
addition of further cations, such as Mn, Ni, Co, Mg.
When the metal surfaces have been phosphated, they
are suitably rinsed with water before they are
aftertreated, e.g., by dipping, spraying, flooding or
rolling by means of the process in accordance with the
nventlon.
The postrinsing agents used in the process in
accordance with the invention may be chemically classified
as

~ ~ 7 ~

aluminum fluorozirconates of low acidity. They may be produced,
e.g., in a process in which metallic zirconium or zirconium
carbonate is dissolved in aqueous hydrofluoric acid so that a
complex fluorozirconic acid is formed. Metallic aluminum or
aluminum hydroxide is then added and dissolved. Whereas that
production process is preferred, the postrinsing agents may
alternatively be produced by other processes.
In another preferred embodiment of the invention the
phosphated metal surfaces are rinsed with aqueous solutions
which additionally contain at least one of the anions benzoate,
caprylate, ethyl hexoate, salicylate in a total concentration
of 0.05 to 0.5 g/l. This will particularly result in a further
increase of the bare corrosion protection. The anions may be
added as the corresponding acids or salts.
The pH value of the postrinsing solutions is
preferably adjusted with cations of volatile bases, which
particularly include ammonium, ethanolammonium and di- and tri-
ethanolammonium.
The passivating postrinsing fluid may be applied to
the phosphated metal surfaces by dipping, flooding, spraying
and wetting, e.g., by means of rollers. The treating times are
between about 1 second and 2 minutes. The fluid may be applied
at a temperature from room temperature to about 80~C.
Temperatures between 20 and 50~C are usually preferred.
Deionized or low-salt water is usually employed to prepare the
postrinsing baths. Waters having a high salt content are less
suitable for preparing the baths.
In another preferred embodiment of the invention the
phosphated metal surfaces are finally rinsed with deionized
water.

,

CA 02018631 1999-01-1~



The process according to the invention is used to
prepare the phosphated metal surfaces for an application of
paint or adhesive. The process improves the adhesion of the
organic films to the metallic substrate, improves also the
resistance of the organic films to a formation of blisters
under corrosive conditions, and inhibits the progress of
subsurface corrosion from damaged portions of the film. The
process has proved to be particularly advantageous in
conjunction with paints applied by cathodic electrocoating
and powder coating or from low-solvent high-solids paints
and paints applied mainly with water as a solvent.
The process in accordance with the invention will
be explained more in detail and by way of example with
reference to the following Example.
Example
Degreased sheets made of steel, electrogalvanized
steel and AlMgSi are sprayed in a manganese-modified low-
zinc phosphating process at 55~C for 2 minutes. The
phosphating solution had the following composition:
0.7 g/l Zn0.04 g/l Fe(III)
1.0 g/l Mn13 g/l P2O5
1.0 g/l Ni2.1 g/l NO3
2.9 g/l Na 0.3 g/l F
0.15 g/l NH40.07 g/l NO2
Finely crystalline, uniformly covering phosphate
layers weighing 2.5 to 3 g/m2 were formed on the three
metal substrates. Thereafter the sheets were rinsed with
water and then subjected to a passivating postrinse. The
passivating postrinsing was effected by spraying at 30~C
for 1 minute. Thereafter the sheets were rinsed with
deionized water and were coated with a primer applied by
cathodic electro-



coating, with a filler and with a top coat. Each paint film wasseparately baked. The total thickness of the coating amounted
to 90 ~m.
The sheets were subsequently scribed by means of a
steel needle as far as to the metal substrate and were then
subjected to various tests. The results are compiled in Tables
1 to 3.
To prepare the postrinsing fluid used in the process
in accordance with the invention, 1.6 g of an aqueous
concentrate containing 0.855% Al + 8.62% Zr + 10.7% F by weight
was diluted with deionized water and was subsequently adjusted
with ammonia to a pH value of 3.5 to 4Ø This resulted in a
postrinsinq fluid containing 0.014 g/l Al + 0,14 g/l Zr
0.17 g/l F + 0.026 g/l NH3.
Control tests were conducted with: A postrinsing
solution containing Cr~VI) and Cr(III), specifically 0.2 g/l
CrO3 and 0.037 g/l Cr(III), and having a pH value of 3.5 to
4.0; a solution of chromium fluorozirconate containing
0.047 g/l Cr(III), 0.083 g/l Zr and 0.121 g/l F and having a pH
value of 3.5 to 4.0; and
a solution containing 0.6 g/l polyvinylphenol and having a pH
value of 3.5 to 4Ø
Each sheet specimen was tested by the salt spray test
in accordance with DIN 50021 SS(1008 h), the Filiform Test in
accordance with ASTM D 2803 (1008 h) and 20 cycles of the
General Motors Test Method TM 54-26 (GM Scab Test). The sub-
surface corrosion under the organic coating (rate of creep
back) was measured in mm.




, ~
~.'

CA 02018631 1999-01-15




TABLE

Results on Steel

Afterrinsing pH- Subsurface corrosion under organic
agent value coating (mm) in
Salt spray Filiform GM Scab
test DIN Test ASTM Test
50021 SS D 2803
(1008 h) (1008 h) (20 cycles)
Cr(VI)- 3.5-
Cr(III) 4.0 0 - < 1 0 3.5

Chromium 3.5-
Fluorozir- 4.0 0 - c 1 0 - c 1 3.5
conate

Polyvinyl- 3.5-
phenol 4.0 0 - 1 < 1 4.0

Aluminum
fluorozir- 3.5-
conate 4.0 0 0 3.5
+ NH3 to pH
(invention)

CA 02018631 1999-01-15
-




TABLE 2

Results on Galvanized Steel

Afterrinsing pH- Subsurface corrosion under organic
agent value coating (mm) in
Salt spray Filiform GM Scab
test DIN Test ASTM Test
50021 SS D 2803
(1008 h) (1008 h) (20 cycles)
Cr(VI)- 3,5-
Cr(III) 4.0 8.5 0 < 1 - 1

Chromium 3.5-
Fluorozir- 4.0 7.0 0 - < 1 < 1 - 1
conate

Polyvinyl- 3.5-
phenol 4.0 6.5 0 - < 1

Aluminum
fluorozir- 3.5-
conate 4.0 5.5 0 < 1 -1
+ NH3 to pH
(invention)




,

CA 02018631 1999-01-15




TABLE 3

Results on AlMgSi
Afterrinsing pH- Subsurface corrosion under organic
agent value coating (mm) in
Salt spray Filiform GM Scab
test DIN Test ASTM Test
50021 SS D 2803
(1008 h) (1008 h) (20 cycles)
Cr(VI)- 3.5-
Cr(III) 4.0 < 1 0 0.5 - 1

Chromium 3.5-
Fluorozir- 4.0 0 0
conate

Polyvinyl- 3.5-
phenol 4.0 0 - <1 0

Aluminum
fluorozir- 3.5-
conate 4.0 0 0 0.5 - 1
+ NH3 to pH
(invention)

A comparison of the data compiled in the Tables
will reveal that the results produced by the process in
accordance with the invention are at least as good in each
case as the best of the three controls which were also
tested.

Representative Drawing

Sorry, the representative drawing for patent document number 2018631 was not found.

Administrative Status

For a clearer understanding of the status of the application/patent presented on this page, the site Disclaimer , as well as the definitions for Patent , Administrative Status , Maintenance Fee  and Payment History  should be consulted.

Administrative Status

Title Date
Forecasted Issue Date 1999-05-11
(22) Filed 1990-06-08
Examination Requested 1990-09-26
(41) Open to Public Inspection 1991-01-28
(45) Issued 1999-05-11
Deemed Expired 2007-06-08

Abandonment History

There is no abandonment history.

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $0.00 1990-06-08
Registration of a document - section 124 $0.00 1990-11-14
Maintenance Fee - Application - New Act 2 1992-06-08 $100.00 1992-06-01
Maintenance Fee - Application - New Act 3 1993-06-08 $100.00 1993-03-18
Maintenance Fee - Application - New Act 4 1994-06-08 $100.00 1994-03-10
Maintenance Fee - Application - New Act 5 1995-06-08 $150.00 1995-06-01
Maintenance Fee - Application - New Act 6 1996-06-10 $150.00 1996-04-11
Maintenance Fee - Application - New Act 7 1997-06-09 $150.00 1997-05-14
Maintenance Fee - Application - New Act 8 1998-06-08 $150.00 1998-05-25
Final Fee $300.00 1999-01-15
Maintenance Fee - Patent - New Act 9 1999-06-08 $150.00 1999-05-20
Maintenance Fee - Patent - New Act 10 2000-06-08 $200.00 2000-05-12
Maintenance Fee - Patent - New Act 11 2001-06-08 $200.00 2001-05-18
Maintenance Fee - Patent - New Act 12 2002-06-10 $200.00 2002-05-17
Maintenance Fee - Patent - New Act 13 2003-06-09 $200.00 2003-05-20
Maintenance Fee - Patent - New Act 14 2004-06-08 $250.00 2004-05-17
Registration of a document - section 124 $100.00 2004-10-06
Maintenance Fee - Patent - New Act 15 2005-06-08 $450.00 2005-05-27
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
CHEMETALL GMBH
Past Owners on Record
GEHMECKER, HORST
HAUFFE, DIETER
KOLBERG, THOMAS
METALLGESELLSCHAFT AKTIENGESELLSCHAFT
MULLER, GERHARD
RAUSCH, WERNER
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Cover Page 1999-05-05 1 50
Cover Page 1994-04-09 1 26
Claims 1994-04-09 3 88
Abstract 1994-04-09 1 28
Description 1999-01-15 9 307
Description 1994-04-09 8 282
Abstract 1998-07-08 1 26
Description 1998-07-08 8 263
Claims 1998-07-08 3 97
Assignment 2004-10-06 4 108
Correspondence 1998-08-31 1 102
Correspondence 1999-01-15 8 249
Office Letter 1990-11-28 1 20
Prosecution Correspondence 1990-09-26 1 29
Prosecution Correspondence 1997-11-21 2 49
Prosecution Correspondence 1997-11-03 6 208
Examiner Requisition 1997-05-27 3 106
Prosecution Correspondence 1993-04-13 3 60
Examiner Requisition 1992-12-09 1 46
Fees 1997-05-14 1 82
Fees 1996-04-11 1 44
Fees 1995-06-01 1 49
Fees 1994-03-10 1 41
Fees 1993-03-18 1 38
Fees 1992-06-01 1 40