Aluminum orthophosphate can be an amorphous aluminum orthophosphate, an orthorhombic aluminum orthophosphate, a mixture amorphous and orthorhombic aluminum orthophosphates at weight percentages ranging from 80 to 20 and 20 to 80, respectively; a mixture of amorphous, orthorhombic, and trigonal (berlinite) aluminum orthophosphates at weight percentages ranging from 10 to 20, 20 to 50, and 20 to 70, respectively, or a mixture of berlinite and orthorhombic aluminum orthophosphate. It is understood that the sum of the individual aluminum orthophosphate percentages must add up to 100 percent. Impurities and/or secondary constituents have not been considered, their relative amount may be 15 weight percentages at maximum, preferably 10 weight percentages at maximum, most preferentially 5 weight percentages at maximum.
Preferred aluminum orthophosphates are amorphous aluminum orthophosphate, mixtures of 60 to 40 wt. % amorphous and 40 to 60 wt. % orthorhombic aluminum orthophosphate, in particular, mixtures of amorphous and orthorhombic aluminum orthophosphate with about equal proportions, as well as mixtures of 20 to 50 wt. % berlinite and 80 to 50 wt. % orthorhombic aluminum orthophosphate, preferentially 20 to 40 wt. % berlinite and 80 to 60 wt. % orthorhombic aluminum orthophosphate. Most preferred is amorphous aluminum orthophosphate.
Aluminum orthophosphates of the tridymite type are not very useful.
At maximum, 1 wt. % water-soluble phosphates and less than 0.05% chloride and/or sulfates may be contained as secondary components. The loss due to heating typically amounts to approx. 1 to 20% the pH value of a 1% suspension is at about 6 to 7.5.
Aluminum orthophosphate according to invention does not essentially contain any aluminum polyphosphates, i.e. their proportion is below 3 wt. %, preferentially below 1 wt. %, and particularly below 0.1%.
Manufacturing of the anticorrosive pigments according to the invention proceeds in an actually known way of converting aluminum salts with phosphoric acid or phosphates, whereby the poorly soluble aluminum orthophosphate is precipitated and separated. For example, aluminum hydroxide can be converted using phosphoric acid, and aluminum sulfate using sodium phosphate. Subsequent drying and, if necessary, tempering and perhaps grinding down to the needed grain size may ensue.
Depending on the conditions prevailing upon conversion of aluminum salt and phosphoric acid or in the process of tempering, the aluminum orthophosphate used according to invention contains more or less large proportions of orthorhombic and trigonal aluminum orthophosphate and may be more or less crystalline.
The conversion may, for example, proceed with aluminum sulfate or aluminum hydroxide. It is possible to add, for example, carbonates such as sodium carbonate in order to adjust the pH value during precipitation. Aluminum orthophosphate precipitates and is filtered off, if required, after further dilution with water. Subsequent drying ensues, for example, by means of spray drying.
If desired, the dried product can be further processed by tempering at 500 to 800° C., preferentially at 600 to 700° C. Tempering normally results in less reactive products which maintain efficacy over a longer period of time. Tempering at high temperatures should be avoided as it has a negative influence on solubility.
If the grain size of the aluminum orthophosphate thus obtained is not fine enough already, grinding and/or sorting or sieving will ensue. The grain size should preferably be in the range of D50 1-15 μm and D90 1-30 μm, whereby D90 lies above D50. In particular, the conditions D50≦10 μm and D90≦10 μm should be fulfilled. It is also preferential if approximately 0.01% of the grains at maximum have a grain size of more than 32 μm. D90 and D50 are defined as follows:
D50 and D90 are values which characterize the particle size of the aluminumphosphate pigments according to the invention, as the pigment particles naturally have different grain sizes. The values are derived from a grain size distribution curve. The value D50 means that 50% of the particles are smaller than 1-15 mm. The D90 value indicates that 90% of the particles are smaller than 1-30 mm.
The packed density lies preferably in the range of 90 to 250 g/l, in case of amorphous aluminum orthophosphate preferably in the range of 90 to 120 g/l.
The anticorrosive pigment aluminum orthophosphate according to invention is suited to replace zinc phosphate in coating agents. It possesses good anticorrosive properties and can be applied in both foundations and top coats.
The composition of coating agents is actually known to the expert. The real formulas depend, among other criteria, upon the subsurface to be coated, the type of coating agent, the intended mode of application, etc. Aluminum orthophosphate is well compatible with most components which coating agents normally contain. Up to about 1 to 20 wt. % aluminum orthophosphate is typically worked into the coating agent. However, if a dilution is foreseen before application, higher percentages may be used, if necessary.
The following examples are intended to further illustrate the invention, however, without limiting it to the embodiments specifically described. All percentages reported refer to weights, if not indicated otherwise.
Phosphoric acid (583 g, 84%, 5.0 mol) is given into a receiver and heated up to approx. 80° C., then aluminum hydroxide (410 g, wet hydrate incl. 5% water, 5.0 mol) is swiftly added, whereby the reaction mixture heats up to approx. 120° C. 500 ml water are brought into the very viscous suspension created. The precipitating crystalline solid substance is aspirated through a paper filter (S&S No. 606 ø110 mm), washed with 65 ml water, and dried over night at 110 ° C. The same amounts phosphoric acid and aluminum hydroxide are then converted for the next batch as described. Dilution proceeds with the mother liquor received in the first batch, then once again filtered, washed and dried. Eight additional batches are produced by analogy to the first run, whereby the mother liquor obtained from the preceding batch is used for making dilutions.
A yield of 6719 g is obtained from all nine batches; this amount is equivalent to a yield of 95%.
Aluminum orthophosphate manufactured in accordance with Example 1 and an aluminum orthophosphate which is supplied under the name of B111 from BK Giulini Chemie GmbH, Germany, and composed of an aluminum orthophosphate which had been made by precipitating aluminum sulfate with phosphoric acid and sodium carbonate, are tempered. To this end, the aluminum orthophosphate is brought into a heat-resistant stainless-steel tube (DIN 1.4841) over a vibrating channel. The tube is situated at a descending angle of 80 mm/1600 mm inside a furnace heated up to 700° C. and rotated at a speed of 10 rotations per minute. The rotations lead the material through the heated zone and discharge it at the end of the tube. The throughput rate amounts to 0.8-1.3 kg/h.
Seven different anticorrosive pigments were worked into a standardized varnish and the varnish was then applied onto sheets of metal. Afterwards adhesion (DIN 53151), degree of blistering (DIN 53209), and subsurface migration (DIN 53167) were determined applying the salt-spray test, the condensation water test, and after wet storage.
ZP10 and Wa 2901 are comparative examples in which, ZP 10 is a zinc phosphate and Wa 2901 a commercially available zinc-free substitute product. The determination of the oil absorption value proceeded according to ISO 787, Part 5.
As to the varnish, two formulas were used. In one, as is common procedure in the paint industry, the amount of pigment was substituted on the basis of an identical oil absorption value. As the oil absorption values of the pigments tested strongly differ, substitution, in the second formula, proceeded on the basis of identical pigment masses in the second formula.
Manufacturing proceeded as follows: item 1 is given into a receptacle; addition of item 2 with incorporation under continual stirring; addition of item 6 under continual stirring, addition of portions of items 7-11 and stirring in using a spatula; pre-mixture of items 2-4 with addition under continual stirring (initially only as much solvent is added so that a viscosity is attained which is appropriate for dispersion, the rest is added after dispersal). Dispersion was done over 60 minutes at a rotation speed of 3300 rpm with 250 g glass beads under cooling.
For application, 500 g stock varnish were thoroughly mixed with 64 g hardener composed of 41.5 g Versamid and 22.5 g xylene. The ready-to-use varnish was diluted with a Xylene-Dowanol PM mixture (4:1) to attain spray viscosity (DIN beaker 4: 16-17 seconds).
Application onto metal sheets proceeded with the aid of high-pressure syringes equipped with a 1.3 mm-nozzle, at 4 bar pressure, to yield a coating thickness: 50±5. Formulations with an identical pigment mass revealed a marked change in flow properties of the stock varnish. The intended coating thickness could therefore not be reached in this test series. In each test, three metal sheets were coated in the wet storage test, salt-spray test, and condensation water test, respectively, in addition to one retention sample sheet. The following tests were conducted after conditioning the specimens in a climate chamber for over ten days:
The results obtained in the adhesion test are compiled in Tables 3 and 4.
It can be conceived that the aluminum pigments according to invention display improved adhesion properties, however, at least an adhesion which is comparable to the reference pigment zinc phosphate (ZP 10). The zinc-free pigment used for reference produced less favorable results.
The results obtained from the test applied to determine the degree of blistering are compiled in Tables 5 and 6.
No differentiation concerning the degree of blistering was obtained in the salt-spray test even after 4 weeks. In the condensation water test, the sheets to which the foundations according to invention were applied, i.e. 1/3, 1/5 and 1/6, as well as zinc phosphate, also did not display any blistering. Intermediate values were obtained for the 1/4 and 1/7 foundations according to invention, whereas the alternative zinc-free foundation 1/2 produced insufficient results. In the wet storage test, only the metal sheets coated with the 1/5 foundation according to invention did not yet display any blistering after a period of four weeks.
Sheets coated with zinc phosphate and the 1/3, 1/6, and 1/7 foundations according to invention, which displayed very small blisters only after the fourth week, produced good results.
However, all metal sheets did equally well within the error margins of the test, except for the alternative zinc-free foundation 1/2.
As a tendency, metal sheets coated with foundations of the second series confirmed the results of the first. Despite the lower coating thickness, all foundations according to invention produced equally good results as zinc phosphate within the error margins of the test, with the exception of 1/3. The alternative zinc-free foundation again produced insufficient.
The results of the subsurface migration test are compiled in Tables 7 and 8.
The least migration was found on the metal sheet coated with the 1/5 foundation according to invention. The subsurface migration values obtained from other sheets ranging between 4.8 and 6.4 were very close to each other, in the order of foundation 1/7, 1/3 and 1/4, 1/6 and reference 1/1/1. The second reference foundation 1/1/2 made an exception.
The metal sheets coated with the foundations of the second series possessing the least coating thickness, sheets coated with the foundations 2/2, 2/3, 2/5 and 2/7 displayed very little migration. Subsurface migration on the sheet with the foundations 2/4 and 2/6 was somewhat better than on the sheet to which the zinc phosphate foundation had been applied.
In summary, the tests demonstrated that the efficacy of aluminum orthophosphate as an anticorrosive pigment is comparable with zinc phosphate which is currently in use. A hitherto available, alternative zinc-free pigment, Pigmentan E, displayed a markedly poorer efficacy.
Number | Date | Country | Kind |
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10 2006 024 869.4 | May 2006 | DE | national |