A CORROSION INHIBITING PIGMENT

Abstract: The pigment is constituted by zinc phosphate dyhydrate or tetrahydrate with an excess of from 0.5 to 6% of zinc oxide over the stoichiometric amount and has the form of rough surfaced spheroids having a maximum dimension lying between 0.5 and 6 microns and a mean size lying between 1.5 and 2.5 microns.

Description: This invention relates to a corrosion inhibiting pigment and to a process for the preparation thereof. The use of crystallised zinc phosphate, either as tetrahydrate or as dihydrate, as a corrosion inhibiting pigment has been known for some time. It is offered on the market in the form of a finely divided white powder, constituted by microscopic crystals having the form of hexagonal slabs which may have a major diagonal dimension of up to 25 µm. This product is used in the preparation of corrosion inhibiting primers forming part of protective coatings for metals. The limitations of this pigment are also known, since it does not give good results in the accelerated prior tests which have to be carried out prior to the approval of any protective coating system. To act, it needs a slow hydrolysis which does not occur during the time the coating is exposed in a salt spray chamber (ASTM B-117). This means that the product is initially rejected in the accelerated prior tests in spite of the fact that it gives good results (effective protection) in long term weather exposure in primers. Many attempts have been made to improve this immediate effectivity by modifying the chemical composition with additions of other substances which, although they accelerate the immediate protective result, at long term suffer from the drawbacks of blistering and loss of adhesion. The above mentioned drawbacks are overcome by a pigment of the type described, characterised in that it is constituted by zinc phosphate dihydrate or tetrahydrate or a mixture of both, with a 0.5 to 6% excess over the stoichiometric amount of zinc oxide in free or mixed crystal form, and in that it is formed by spheroids having a rough surface, the maximum dimension of which lies between 0.5 and 5 microns, with a mean size lying between 1.5 and 2.5 microns. The process for manufacturing said pigments comprises the following steps of: suspending zinc oxide in water; finely dispersing the zinc oxide in water until the said oxide is partly converted into zinc hydroxide, giving a dispersion; dissolving phosphoric acid in water, giving a solution; adding an organic or inorganic anion ammonium salt to the dispersion or solution; simultaneously pouring the dispersion and the solution in a reactor such that there is always a considerable excess of zinc oxide therein, the zinc oxide reacting with the phosphoric acid; the zinc phosphate is gradually formed in the midst of a vigorous shearing action, giving a small size precipitate; washing until removal of said anion salts; and drying, to give a pigment constituted essentially by zinc phosphate dihydrate and/or tetrahydrate, with 0.5 to 6% excess of zinc oxide over the stoichiometric amount, formed by rough-surfaced spheroids having a maximum dimension lying between 0.5 and 5 microns and a mean size of 1.5 to 2.5 microns. It was not foreseeable that on modifying the physical parameters of a powdered zinc phosphate, the new product would have a behaviour, when incorporated in corrosion inhibiting coatings, much better than that of the conventional pigment, although an attempt were made in the latter to optimise the mean particle size to avoid them from being either too large or too small. Nevertheless, the product obtained according to the invention represents a clear advance with regard to corrosion inhibiting effectivity, adherence and blistering of the protective film, which is evidenced by salt spray and distilled water immersion tests at 50°C. Reference is made hereinafter to the drawings accompanying the specification allowing a better understanding. In the drawings: Figure 1 is a front view of a cold rolled carbon steel sheet to which there has been applied a first sample of a paint prepared with conventional zinc phosphate pigments. Figure 1 a is a similar view to the previous one, although the paint has been prepared with zinc phosphate pigment according to the invention. Figure 2 is a front view of a sheet to which there has been applied a second sample of paint prepared with conventional zinc phosphate pigments. Figure 2 a is a similar view to the previous one, although the paint has been prepared with zinc phosphate pigments according to the invention. Figure 3 is a view 5,000x of conventional zinc phosphate particles. Figure 4 is a view 5,000x of zinc phosphate particles according to the invention. Figure 4 a is a view of a particle with a greater degree of magnification. Figure 5 is a front view of a sheet to which there has been applied a third sample of paint prepared with conventional zinc phosphate pigments. Figure 5 a is a view similar to the previous one, although the paint has been prepared with zinc phosphate pigments according to the invention. Figure 6 is a front view of a sheet to which there has been applied a fourth sample of paint prepared with conventional zinc phosphate pigment. Figure 6 a is a view similar to the previous one, although the paint has been prepared with zinc phosphate pigments according to the invention. In Figures 1 and 1 a , the first paint sample had an oil long alkyd resin (Synolac 503 x 60) as vehicle and a pigment concentration of 35% by volume, 27wt% of the pigment being corrosion inhibiting (active); the dry paint film thickness wss 33 µm; only one coat of paint had been applied and the cuts 2 had been made. The drawings illustrate the results of 400 hours exposure to salt spray. after which cross cuts 3 were made and the paint was peeled off with adhesive tape (left upper portion 4). Subsequently the coat of paint was removed from the righthand side 6 of each test specimen with paint remover, allowing the degree of attack on the substrate to be better observed. The test specimen of Figure 1 a may be seen to have suffered less attack and that the adherence is better, since the cross cut portion 3 has not been peeled away. In Figures 2 and 2 a , the binder is an epoxy resin and polyamide in a ration of 1.7 : 1, with a pigment concentration of 28% by volume, with 100% being active pigment, the dry paint coat thickness being 34 µm. The deterioration exhibited by the sheet of Figure 2 (with conventional zinc phosphate pigments) is noticeably greater than that of the sheet painted with paint containing pigments according to the invention. The paint system is single coat and the Figures also illustrate the results of 400 hours exposure to salt spray. In this case, the paint was not peeled off. In Figures 5 and 5 a , two paints with linseed oil long alkyd resin (Synolac 503 x 60) and a 63 wt% solids content, a pigment concentration of 35% by volume, 27 wt% of the pigment content being active, were applied. The system was single coat and had a dry thickness of 33 µm. In Figure 5 the active pigment was conventional zinc phosphate and in 5 a it was zinc phosphate according to the invention. After applications on cold rolled steel sheets, previously degreased and cleaned of rust and after exposure to salt spray for 240 hours, the adherence to the test specimen prepared with the conventional pigment was seen to be less and that the attack on the area where a cut was made was also greater than in the test specimen with the pigment prepared in Example 1 to be described hereinafter. In Figures 6 and 6 a , cold rolled steel test specimens to which an epoxy-polyamide primer and a polyurethane finish coat have been applied are shown. Hereinafter a table is given with the results obtained in immersion tests. The different degree of adherence of the conventional pigment in comparison with the new product may be seen in Figures 6 and 6 a . While it was possible to peel off the whole coat in the case of the former, in the latter it was possible to peel off, discontinously, only a sixth part of the film after 60 seconds. Figure 3 is an illustration of pigments constituted by conventional zinc phosphate. Under the microscope, it is seen to be formed by very flat truncated pyramids, joined together at the base, virtually forming square or hexagonal slabs of a generally flat surface, although there are cracks, dislocations and some irregularities. The size may be taken to lie between 4 and 25 microns, with a mean size of about 6 microns. In the case of a pure tetrahydrate, it is crystallised in an orthorhombic system, with a Hopeita structure. It may also be a dihydrate if the final drying temperature is above 115°C. The commercial product is usually a mixture of di- and tetrahydrate, with one predominating over the other. In long duration tests, these pigments give satisfactory results. Figure 4 is an illustration of pigments constituted by zinc phosphate according to the invention, containing a small amount of free zinc oxide (between 0.5 and 6%). The crystalline structure is that of a tetrahydrate with some dihydrate, but in X-ray diffraction it substantially appears as a less perfect crystallization than the conventional one. The small size of the monocrystals and their irregular disposition means that less accumulated refractions of the crystal planes fulfilling Bragg's condition are obtained. The scanning electron microscope photographs show spherical spores having diameters of from 0.5 to 5 microns, with a mean diameter of 2.5 microns. The surface of these spores is irregular, formed by small lamellar hexagonal crystals having a diagonal of 0.05 to 0.5 microns, disposed more or less radially. The large surface area exhibited by these spheroidal forms, the exterior of which is constituted by an infinite number of lamellae implanted perpendicularly to the tangent in all directions, substantially increases the oil absorption and therefore the active surface, an example of which is the fact that the conductivity of a suspension in distilled water at 25°C is from 4 to 5 times higher than that of a normal zinc phosphate. I.e., while a conventional zinc phosphate pigment, after thorough washing with distilled water, has a conductivity of 30 to 50 µS/cm, the pigment according to the invention has a conductivity lying between 120 and 350 µS/cm when the conductivity is measured according to ASTM D 2448-73. Immediately after precipitation and during drying, the spheroids form lumps which are easily broken apart by micronization, being reduced to the original spheroids. To summarise, the pigment of the invention is distinguished from the conventional one in the form of the elementary particles, mean size, size distribution and specific area. All of this provides for increased reactivity, making this new pigment more effective in the salt spray tests. conferring greater adherence to the paint films, improving the resistence to blistering and a better behaviour in the immersion tests. In a determination according to ISO/R 787, the pigment of the invention exhibited an oil absorption of from 55 to 95. A chemical analysis of the product of the invention in comparison with a conventional one is as follows: Conventional zinc phosphate Zinc phosphate according to Ex. 1 Moisture at 10°C, % 3 6 Loss at 550°C, % 9.7 12.1 Zn content on calcined product, % 51 53 Soluble salts, % 0.23 0.28 Conductivity at 25°C, µS/cm 86 428 pH aqueous extract 6.9 7.8 Residue in seive at 44 µm, % 0.06 0.1 Oil absorption 15 to 20 76 to 83 In the Examples described below, ammonium chloride or nitrate is used an ammonium salt. Nevertheless, the use of these salts is not exclusive and ammonium acetate, tartrate, phosphate or any other ammonium salt may be used. Even ammonium hydroxide could be used, but it is not used for reasons of economy, in view of its basic nature. Also for reasons of economy, it is not recommended to use zinc chloride and trisodium phosphate as reactants in the presence of an ammonium salt in the preparation of these products. In this case there is also the difficulty of exhaustively washing out the sodium chloride formed in the reaction. EXAMPLE 1 On the one hand, a thick paste was prepared with 168 kg of zinc oxide finely dispersed in 850 l of water at 60°C. The dispersing action has to be very energetic and, therefore, the aid of a powerful mechanical disperser is absolutely necessary. This action must be sufficiently energetic to allow the oxide to become activated, i.e., partially converted into hydroxide, so as to facilitate the following reaction. In a separate container, appropriate for containing acid, a mixture of 85 l of phosphoric acid (d=1.640) with 67 kg of ammonium chloride diluted to 350 l, also under heating to 60°C, was prepared. The two fluids were poured together in a continuous reactor stirred with flowrates adjusted appropriately to leave always a considerable excess (0.0576 g/ml) of zinc oxide. The reactor stirrer must be a high powered machine having a peripheral speed of 20 to 35 m/sec. The pouring time should lie between 30 and 40 min. The starting temperature of 60°C may reach 80°C at the end of the pour. Normally, at the end, some phosphoric acid solution was left over and had to be poured alone, since the zinc oxide paste was exhausted first. The precipitate develops by stirring for about 40 minutes and the final pH is adjusted to 7. The mixture was filtered and washed to remove the chlorides and was dried at 95-100°C. Finally, 270 kg of a particular product formed by spheroids covered by small lamellar crystals having a behaviour and characteristics similar to those described above was obtained. The yield is not stoichiometric, due to the zinc which remained in solution in the mother liquors. The behaviour of the pigment prepared according to the above Example in salt spray tests was described above when describing Figures 5 and 5 a . To check the results obtained with immersion tests, paint systems comprising an epoxy-polyamide primer and a polyurethane finish on cold rolled sheet steel test specimens were prepared. The primer was formed by: a mixture of epoxy and polyamide resins at a ratio of 1.3 : 1 with two volumetric pigment concentrations (V.P.C.) of 25% and 35% and 100% active pigment. The paints were applied at two thicknesses of 15 and 30 microns for each V.P.C. The finish coat was polyurethane based (two components) pigmented with titanium bioxide with a V.P.C. of 16% and a thickness of 75 microns when dry. The painted sheets were immersed in distilled water at 50°C for four days. The results obtained after this test are summarised in the table, evaluating blistering, time required to peel the film, which time is in direct relationship with the adherence and corrosion stains. As in the previous cases, the tests were run on conventional pigment and with the pigment of the invention. The table shows that the protection difference is greater at thin dry film values and at lower volumetric pigment concentrations. The difference of adherence between the conventional pigment and that of the new product is shown in Figures 6 and 6 a , as stated above. EXAMPLE 2 An aqueous suspension of 168 kg of zinc oxide with a total volume of 800 l was prepared. It was activated and 40 kg of ammonium chloride were added, the temperature was held to room temperature (15 to 20°C). Separately 87 kg of phosphoric acid (d=1.628) were dissolved in water to 300 l, the temperature being held at room temperature. The suspension and the solution were poured simultaneously in a stirred continuous reactor. The reactants entered at the bottom of the reactor and the reacted product was removed by overflow. The temperature was held at 20°C. Pouring lasted 20 minutes. The product was allowed to develop for 30 minutes. The product was decanted and washed to complete removal of chlorides, i.e., a conductivity of 70 microsiemens. It was filtered and dried at 100°C. After grinding, the product had a similar appearance under the microscope to that of Example 1 and behaved in a similar way when incorporated in paints. EXAMPLE 3 In this Example, the pigment was prepared under the same conditions as in Example 1, but using ammonium nitrate instead of the chloride. The product obtained exhibited similar physical characteristics, but the SEM photographs obtained showed that the elementary crystals forming the spheroidal spores were larger than when ammonium chloride was used. This was confirmed by X-ray diffraction in which the Hopeita structure predominates over the others. The physical and chemical behaviour of this pigment was the same as that of Example 1.

Claims: 1.- A corrosion inhibiting pigment, characterised in that it is formed by zinc phosphate dihydrate or tetrahydrate or a mixture of both, with an excess over the stoichiometric amount of from 0.5 to 6% zinc oxide in free or mixed crystal form, and being formed by spheroids having a rough surface the maximum dimension of which lies between 0.5 and 6 microns and having a mean size between 1.5 and 2.5 microns. 2.- The pigment of claim 1, characterised in that said rough surface is formed by zinc phosphate lamellar microcrystals having a maximum dimension lying between 0.05 and 0.5 microns, disposed generally radially. 3.- The pigment of claim 1, characterised in that it has an oil absorption between 55 and 95 when determined according to ISO/R 787. 4.- The pigment of claim 1, characterised in that, after washing with distilled water, it exhibits a conductivity of 120 to 350 µS/cm when determined according to ASTM D 2448-73. 5.- A corrosion inhibiting coating characterised in that it comprises a pigment according to claims 1 to 4.

Inventors: AUBAREDA, VALLVEY, JUAN, LEBLANC FRANCIA, OSCAR, MARTORELL SOLE, CARLOS, Martorell Solé, Carlos
Applicants: COLORES HISPANIA S.A.
Application year: 1988
Main classification: C09C1
IPC codes: C01B25, C09D5, C09C1