Patent Application
20070199479
The invention relates to a fine-particle, bright, and highly opaque rutile-based pigment without the addition of impurities by reactive metal components and to a method for the production of such pigments.
Nickel antimony titanium yellow pigments are by nature pale yellow pigments with high opacity. Overdyeing, i.e., over-coloring, with high quality organic pigments makes it possible to obtain highly saturated full-tone colors with which the entire color spectrum can be covered, with the exception of blue and violet hues. This overcoloring results in a synergy between the relatively high opacity of the cost-effective nickel antimony titanium yellow and the great color intensity of the organic overcoloring pigments, which are generally quite expensive.
This effect can also be obtained using titanium white; however, overcoloring always leads to greater brightening, that is, to less saturation, due to the high whitening power of titanium white pigments. Another disadvantage of titanium white overcoloring is the photocatalytic effect of titanium white pigments, which leads to a sharp decrease in the light-fastness and weather-fastness of the expensive organic color components. Consequently, full hues based on titanium white “age” some four-times faster than mixtures of the same organic color components with nickel antimony titanium yellow.
In the past, this decisive use of nickel antimony titanium yellow was seldom used because the nickel titanium pigments currently available on the market are abrasive (grain-hard and sharp-edged), have poor gloss, and are inferior in terms of covering capacity compared to titanium white. Moreover, the following economic background should be considered:
Nickel antimony titanium yellows account for relatively small market shares among titanium pigments, as the following figures demonstrate: titanium white world market: 4,000,000 tons, titanium yellow world market: 20,000 tons, of which chromium antimony titanium yellow: 16,000 tons, of which nickel antimony titanium yellow: 4,000 tons.
The annual tonnage of chromium antimony titanium yellow is disproportionate to that of nickel antimony titanium yellow. As colored pigments, nickel antimony titanium yellows offer merely an unsatisfactory option for replacing the 100,000 annual tons of lead sulfochromate and molybdate red pigments pursuant to the hazardous materials laws and environmental protection laws that have become increasingly stringent since 1980. The reason for this is the deficiencies, considered unchangeable, that are manifested in particular by the inadequate opacity, compared to titanium white and to chromium and cadmium yellows and by inadequate gloss and high abrasiveness.
These three deficiencies are the result of one and the same cause, specifically a mean particle size, primarily of the nickel antimony titanium yellow, that is too large and that is an average of 1000-2000 μm in the best qualities found on the market, while the optimum opacity of a pigmentary coloring agent is attained with a particle size of 300 μm and with optimized grain shape and surface. A pigment loses about 20% of its opacity when the mean particle diameter is greater than 500 μm. Finer commercial types according to the prior art are regularly slightly doped and greatly whitened, and in addition due to their high grinding costs expensive, highly doped, high-fired products are unknown because they are inconsistent in terms of color.
Surface enlargement when the mean particle diameter is 300 μm should be avoided for color pigments because they become transparent when they drop below a particle diameter of about half the wavelength of the light reflected by them, which is undesirable for applications for nickel antimony titanium yellow pigments. When the hardness of the particles is high, abrasiveness increases for spiky and sharp-edged particles. The goal is therefore also to produce isometric particles (rhombi) that are chamfered or have beveled flattened or rounded areas on the corners. This cannot be obtained using a coating in accordance with DE-A-2 936 746 that acts in cooperation with surfactant agents such as a slip agent and which additionally requires its own processing step and the use of auxiliary agents as the subject matter of the invention. Nevertheless, for avoiding color effects under different types of illumination (metamerism), a relatively smooth surface and also approximate uniformity of the (projected) edge lengths should be obtained; a spherical shape is unattainable under any conditions, however.
Taking the aforesaid into account, the relevant prior art shall be addressed:
In the past, a mean particle size of 300 nm has not been reached by any manufacturer with satisfactory results for highly doped and/or fully annealed nickel or chromium antimony rutile yellow pigments (TiO2<87%). Patent DE-A-3 202 158 describes in particular chromium antimony titanium yellows. In fact, the small dopings described therein inter alia with antimony and chromium at low firing temperatures <1000° C. with subsequent wet grinding in bead mills lead to a pigment with a narrow grain size distribution and corresponding fineness, sometimes also due to the softer grain of the mixed phase oxide pigments described therein. However, there are still also limits for hue creation in terms of how the reactive iron content can assume uncontrollable amounts if a non-metallic mill with resistant lining is not used as it is inventively in this case. Still, with a product according to the prior art in DE-A-3 202 158, increased photoactivity, and with appropriate very fine grinding, a high degree of whitening must be accepted. If iron abrasion is permitted in the milling process, the material grays and leads inter alia to disturbances in PVC-based matrices. This is true even for mixed phase rutile-based oxide pigments that contain iron bound as a non-reactive component in the crystal lattice of the rutile, as in example 3 of DE-A-3 202 158.
In accordance with the teaching of DE-A-3 202 158, a coloristically favorable grain size distribution is attained when low doping, relatively low firing temperature, and wet milling are combined. However, this application does not provide any information on grain size distribution and specifies the type of milling only imprecisely.
In the case of titanium dioxide, synthesis during the chloride method with the adjustment of the TiCl4 burner and mixing in of agglomeration-preventing sand in the subsequent cooling and conveying process has already found a practical path for adjusting optimized particle size distributions (d50=approx. 280 nm for light of 550 nm wavelength) (see inter alia: Winkler, J: “Titanium Dioxide”, Hannover: Vincentz, 2003; ISBN 3-87870-148-9; pp. 35-37; 51-58). Although in this method small quantities of aluminum chloride are metered to the titanium tetrachloride for “rutilization”, it being unresolved how many lattice places in the rutile are really occupied by aluminum ions, this method is not promising e.g. using the addition of antimony and nickel chlorides to titanium tetrachloride upstream of the burner. Separation and inhomogeneous volatility of metal chlorides and metal oxychlorides prior to the lattice insertion of the metal ions is observed. A lengthy afterglow period leads to reagglomeration.
The Ishihara Company is particularly active in the prior art. This is demonstrated by worldwide patent applications. These include for instance EP 1 245 646 (A1, corresponds to U.S. Pat. No. 6,576,052), in which a fine-particle TiO2 obtained from the chloride process, already 100 to 400 μm mean grain size, is re-ground to a corresponding fine primary grain size during a siloxane post-treatment and coating with aluminum phosphate using a jet mill. According to EP-A-1 273 555 (corresponds to U.S. Pat. No. 6,616,746), the same grain fineness of the raw pigment for coating is used with multivalent alcohols and hydrolyzed amino silanes and/or aluminum hydroxide. The procedure is the same as the foregoing. Good dispersibility of the photostabilized products is claimed. For grinding, the pigment is comminuted after or during addition of the coating and stabilization reagents at a temperature of 120 to 300° C. in a jet mill or a similar “fluid energy mill” that permits a hydrolysis reaction of the amino siloxanes and other reactive components and prevents any reagglomeration during the coating process. This patent relates only to TiO2 in rutile modification (which is preferably formed by the additions of aluminum). After working up the batch, the coating is principally to act in a manner that prevents agglomeration and is photostabilizing, i.e. lastingly moderates the photocatalytic effects of the pigment.
Wet grinding of rutiles, that is also rutile yellow pigments, in high-intensity bead mills is prior art e.g. in accordance with DE-A-3 930 098. These are sold by a number of different specialty companies.
The option provided e.g. in DE-A-4 106 003 to obtain an a priori finer grain structure and thus save a grinding process by “alloying” the firing batch for a rutile brown pigment with small quantities of cerium, inter alia, cannot be performed with chromium and nickel titanium pigments due to the brighter hues that are more sensitive to fluctuations in doping.
Basically many companies seem to prefer wet precipitation to the actual synthesis of the pigment and thus create a “wet precursor” which is imprinted with the grain distribution and thus the fineness, which is maintained even until after calcination and final fine grinding. The hydroxyl groups on the surface of the freshly precipitated oxides and hydroxides represent a good precursor for the diffusive penetration of the rutile lattice, which also has numerous vacancies, with foreign metal ions after evaporating the water above 150° C. However, the finer grain sizes possible due to the lower firing temperature are not of reproducible color intensity. The diameter still fluctuates between 800 and 1200 μm.
Proceeding from the prior art described in the foregoing, the object of the invention was to obtain a fine-particle, bright, and highly opaque rutile-based pigment that is distinguished by superior opacity, gloss, and lower abrasiveness. Moreover, it should have the smallest possible or no iron content, for instance in the ppm range in any case. Moreover, the invention should provide a method with which such a pigment can be produced in a particularly economical manner.
This object is inventively attained using a fine-particle, bright, and highly opaque rutile-based pigment that is characterized in that it has a grain size distribution with particle diameters between 50 and 1000 μm and for mono-, bi-, tri-, or oligomodal frequency distribution has a primary maximum between 230 and 400 μm, whereby for a bi- or multimodal frequency distribution where necessary a secondary maximum occurs, at less than 25% of the primary maximum, between 400 and 1000 μm, in particular between about 400 and 900 μm. It is particularly preferred when the claimed primary maximum is between 280 and 340 μm and/or the secondary maximum is between 480 and 800 μm. Furthermore, it is preferred when the mean particle diameter of the pigment is between 80 and 1000 μm, in particular between 80 and 900 μm. The range of 120 to 600 μm is very particularly preferred. Moreover, in individual cases it is advantageous when the pigment has an asymmetrically shaped monomodal frequency distribution for the particle diameter with a maximum between 250 and 390 μm, in particular between 280 and 340 μm.
As is consequently evident, the particle size for the type described should be considered an essential feature of the present invention. This shall be explained in greater detail in terms of the technology. Surprisingly, it has been demonstrated that the sharp grain size distribution must sit on a “base”, which as needed can also have secondary maximums in the amount of up to 15%, primarily 5%. Without this explanation being limiting or exhaustive, this special embodiment of a sharply asymmetrical, bi- or oligomodal grain distribution or a “deep drag” for attaining optimum brightness and saturation can be traced back to the need for providing optimum space filling in the matrix by approaching a specific portion of the pigment on the “Fuller curve”. As long as they remain the minority, the finest portions in small diameters (150 μm<D<250 μm) themselves can certainly cause the absorption edge of the pigment to be steeper due to stronger absorption, which likewise causes intensification of the Raleigh scattering, resulting in improved brightness.
The grain shape must also receive the required “polishing” in order to be able to work itself optimally into a matrix, improve the gloss, and protect the normal application tools. This can be done effectively and in the same work step in the inventive method, which will be described in the following, by adding auxiliary agents. The grain surface is abraded, using the selected method and appropriate additives and coatings, to the round shape, which helps to moderate the abrasiveness of the particles and to improve the flowability of highly-pigmented preparations in later use. The tendency of fine rutile pigments to agglomerate is now effectively addressed during creation, i.e., in the grinding batch, which will be described in greater detail.
The invention includes in particular the following pigments: a highly doped, fully annealed nickel antimony rutile yellow, a chromium antimony rutile yellow that is just as highly doped and fully annealed, and a titanium dioxide, preferably made of synrutile precursors, each in rutile structure, that is just annealed and only weakly doped with foreign parts.
The inventive fine-particle, bright, and highly opaque rutile-based pigments also result in excellent gloss values. A pigment in accordance with the invention is distinguished in that it has a 20° reflectometer gloss value of at least 42 according to DIN 67 530 and a 60° reflectometer gloss value of at least 80, in particular a 20° reflectometer gloss value of at least 50, in particular 55 to 70, and a 60° reflectometer gloss value of at least 83, in particular 83 to 93. The excellent covering power of the claimed pigments is particularly valuable. These are distinguished in that the covering power in accordance with DIN 55 987 is greater than 100% relative to a standard rutile pigment comparison substance, in particular is greater than 110%, and in particular is between 115 and 130%. Neither dry grinding used today as the state of the art nor conventional sand/bead mills are suitable for producing the inventive pigment of the type characterized.
The present invention also proves to be valuable because it no longer has any regular increase in remission across all wavelengths, due to the sharpness of the grain size distribution, but rather has a maximum in the yellow range of the spectrum (about 570 to 600 μm). This simultaneously prevents the b* values from decreasing excessively because then the brightness (that is, the non-wavelength-specific remission) would increase excessively.
Other objects and advantages of the invention will become more apparent upon reference to the following Specification and annexed drawings, in which:
The subject matter of the present invention is also a method for producing the pigments in accordance with the invention. It is characterized in that an inorganic mixed phase oxide pigment with rutile structure is treated by means of high-speed grinding in an aqueous suspension in an agitator ball mill with resistant lining until the grain size distribution described in the foregoing has been attained. Preferably the grinding unit and the grinding tools have a wear-resistant and inert coating. Preferably the resistant lining material for the (high-speed) agitator ball mill is an inert and wear-resistant ceramic material, in particular in the form of a heat-conductive ceramic material for assisting in cooling. Alternatively, it is preferred that the resistant lining material for the agitator ball mill is an inert and wear-resistant plastic, e.g. polyurethane.
Additional information regarding the method. It is preferred that resistant grinding pearls with a diameter of about 0.2 to 1.7 mm, in particular from about 0.5 to 1.2 mm, are used in the milling unit in an analogous manner for coating. The temperature during fine grinding is preferably between about 20 and 90° C., in particular between about 40 and 60° C. Moreover, it is useful that the fine grinding is performed in the framework of the inventive method using a recirculation method, the mean dwell time of the ground material in the agitator ball mill being 4 to 44 min, in particular 10 to 18 min. It is useful that the circumferential speed of the rotor in the agitator ball mill is 5 to 19 m/s, in particular 10 to 12 m/s. In addition, in the framework of the invention the fill level is usefully planned to be advantageous. It is preferred that the fill level of the agitator ball mill with grinding bodies is about 60 to 90 vol. %, in particular about 70 to 80 vol. %.
In an exceptional case, it is preferred that pre-comminution occurs upstream of the inventive method. This usefully occurs in a ball mill, likewise made of resistant material, metal contact with the ground material being largely prevented. This is one reason that iron content is largely prevented in the inventive pigments. In other words, this means that the iron content is determined solely by the parameters of the raw materials and is thus in any case in the ppm range.
Regarding the history of the inventive method it should be stated: After initial experiments with highly doped and fully annealed nickel titanium yellow as for the teaching of DE-A-3 202 158 with high-speed agitator ball mills failed due to unsatisfactory color consistency, it was surprisingly found that the grinding efficiency improved dramatically in connection with chemically and mechanically resistantly lined agitator ball mills and ceramic fine grinding bodies. Preferably the lining should be non-metallic. It could comprise plastic, but it could also comprise ceramic. Therefore a sharp grain size distribution with about 320 nm mean particle diameter, close to the optimum, can be attained with relatively low grinding complexity, the grain size distribution additionally also having a steep course that conforms to the objective. The refitting of the agitator ball mill, mentioned in the foregoing in terms of the metal-free lining, was thus extremely important for conducting the new inventive wet milling method successfully. The inventive pigments and also the inventive method have particular value, which is evidenced by numerous advantages: for instance, the grinding efficiency can be promoted using the surfactant polymers, mentioned in the foregoing, specifically using differently substituted polysiloxane compounds and polar substituted long-chain alkanes. The polysiloxanes primarily effect hydrophobization of the per se polar surface of the inorganic pigment particle. During subsequent working in into nonpolar binding agents (solvent-containing resin) or other polymer materials (polyolefins), the hydrophobization of the pigment surface leads to clearly more rapid rewetting and thus to less wear. Under the selected grinding conditions, highly disperse oxides of silicon or aluminum prove to be the solution to hydrodynamic problems, in addition to adjusting an optimal ion strength and therefore viscosity with a salt of an oxygen acid of for instance sulfur or phosphorus. Using the aforesaid compounds it is therefore possible to obtain particularly advantageous controllability when optimizing the inventive method.
The present invention overcomes the aforesaid deficiencies of prior art nickel antimony titanium yellow pigments and leads, optionally using a modified finish process, to yellow pigments with substantially improved opacity and substantially improved gloss that is the equivalent of that of titanium white; at the same time the color intensity is improved compared to low-doped rutiles that are annealed at lower reaction temperatures, which is clearly evidenced in
The advantages of the inventive pigment can be depicted as follows: It is distinguished from the prior art product by improved gloss, low whiteness/less brightening, relatively high color saturation, and extremely high covering power, not usable in the past in this class of material, with low photoactivity for fine-particle rutiles compared to the prior art. Furthermore, in practice it does not demonstrate any disadvantageous abrasivity or any interaction of any grinding residues with the application matrix. In particular it is essentially free of reactive metals or metal compounds, in particular reactive iron compounds.
The known methods attain only mean particle sizes of 600 to 1200 nm, which results from the curves in enclosed
As compared to the conventional product that is usually jet milled, an example of which is shown in
The invention shall be explained in the following in greater detail using various examples, although this shall not be construed as a limitation.
It is advantageous to have a conventional pre-comminution step upstream of fine grinding in order to limit the duration of grinding. This can occur according to the following variations, and the ground material is then fed directly to the inventive process (these are actually processes in accordance with the prior art, which are only included for the sake of completeness and to demonstrate the general applicability of the invention):
Ball Mill/Roller Block
40% suspension (4 kg pigment and 6 L water) of the raw pigment is ground with 25-mm ceramic balls on the roller block for 60 to 90 minutes.
Sand Mill:
Horizontal PU-lined sand mill with Ottawa sand or zircon silicate grinding beads (Rimax) with a diameter of 2.5 to 2.8 mm. There are 1 to 2 passes with 600 to 800 kg 40% suspension per hour. The temperature must be kept below 60° C.
Although a jet mill for dry pre-comminution with subsequent slurrying of the raw pigment to the 40% suspension is very effective and does not cause any wear, it is very complex and time-consuming to manage and is therefore expensive.
Corundum disc mill: Pre-comminution of the raw pigment particles into a 40% suspension has a throughput that is too low, but can be used trial-wise.
The 10 kg of the 40% suspension of the nickel titanium raw pigment from Example 1 are adjusted to a pH of 6-6.5 with 10% sulfuric acid, and if necessary adjusted to conductivity of 2000 to 2500 μS/cm by adding sodium sulfate solution, in order to obtain a stable, pumpable suspension having a viscosity of 600-700 mPa*s. A Lehmann “FM 20” mill lined with a special heat-conductive ceramic material for cooling is used.
The suspension is pumped through the mill 3 times, passes 1 and 2 with grinding balls (cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L) 1.7 to 2.4 mm, the third pass with grinding balls 0.7 to 1.2 mm (cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L) at a throughput of 600 g suspension per minute; this is equal to a dwell time of 130 to 150 sec per pass, that is, a total dwell time of 10 min. The mill is set to a circumferential speed of 12 m/sec. The grinding temperature is no more than 45° C.
1 pass with grinding balls (cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L) 1.7 to 2.4 mm (72 vol. % of the grinding space), then circulatory grinding for 30 to 60 min with a throughput of 900 g suspension per min, which equals total dwell time of 6 to 12 min and 4 to 8 theoretical passes. It is necessary to check the pH after each pass or every 30 min during circulatory grinding. If the pH rises above 6.5, it must be corrected by adding sulfuric acid. The mill is set for a circumferential speed of 11 m/sec.
After 45 minutes have elapsed, 20 g (0.2%) Nuosperse 2008, a fatty amine salt of an ethoxylated and partially phosphatized polymer oleyl alcohol are added for conditioning and grinding continues for an additional 15 min. If the suspension becomes thin, the viscosity must be raised by adding no more than 50 g sodium dihydrogen phosphate, and if necessary more additional sulfuric acid. The grinding temperature is no more than 45° C.
After fine grinding in accordance with Example 2b, the pigment is washed until the conductivity of the excess liquid is 500 to 800 μS/cm. The suspension is concentrated by means of centrifuge decanter or filter press to a solid content of 55 to 65%. Then additional 2.5% sodium sulfate is added to the slurry, the viscosity is adjusted to 620 Pa*s with equal parts by weight of sodium phosphate and sulfuric acid, an additional quick pass (dwell time <60 sec) through the mill is performed with grinding balls (cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L) 1.7 to 2.4 mm.
An excellently covering yellow pigment is obtained that has optimum gloss in the coating. There are no detectable differences between the pigment in accordance with the method in Example 2A and in accordance with the method in Example 2B.
After fine grinding in accordance with Example 2b, the pigment is washed until the conductivity of the excess liquid is 500 to 800 μS/cm. The suspension is concentrated by means of centrifuge decanter or filter press to a solid content of 60%. Then additional 3% non-ionic, modified fatty acid derivative (commercial product) and 100 g “Aerosil” are added to the slurry, and an additional quick pass (dwell time <60 sec) through the mill is performed with grinding balls (cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L) 1.7 to 2.4 mm (same filling as before).
An excellently covering yellow pigment is obtained that has optimum gloss in the coating. It is not possible to detect a feared matting effect from the Aerosil There are no detectable differences between the pigment in accordance with the method in Example 2A and in accordance with the method in Example 2B.
After fine grinding in accordance with Example 2b, the pigment is washed until the conductivity of the excess liquid is 500 to 800 μS/cm. The suspension is concentrated by means of centrifuge decanter or filter press to a solid content of 60%. Then additional 2% a [sic] polydimethyl siloxane (aqueous emulsion) is added to the slurry to reduce abrasivity, in addition 35 g “aluminum oxide C” from the Degussa Company (commercial product), an additional quick pass (dwell time<60 sec) through the mill is performed with grinding balls (cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L) 1.7 to 2.4 mm (same filling as before).
After separation, an excellently covering, bright yellow pigment is obtained that has optimum gloss in the coating. There are no detectable differences between the pigment in accordance with the method in Example 2A and in accordance with the method in Example 2B.
To illustrate how independent the pigment properties are in accordance with this invention, deviating from the wording of these examples the following auxiliary agents are used in variations that are reasonable to experts in the field without this having a significantly further improving effect on the result, in contrast to DE-A-2 936 746:
Modified Fatty Acid Derivatives
1. Fatty amine salt of a polymer oleyl alcohol, ethoxylated and phosphatized, and
2. Non-ionic, modified fatty acid derivative
Polysiloxane Compounds
1. With polyether group-modified siloxane
2. Alkylaryl-Modified Polysiloxane
Nanodisperse Aluminum Oxide or Silicic Acids
Aluminum oxide C (Degussa)
Aerosils
The following can be used as grinding balls:
1.7 to 2.4 mm cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L
0.7 to 1.2 mm cerium-stabilized zircon oxide balls, bulk density 3.7 kg/L
0.6 to 0.8 mm yttrium-stabilized zircon oxide balls, bulk density 3.6 kg/L
0.8 to 1.0 mm yttrium-stabilized zircon oxide balls, bulk density 2.8 kg/L
2.5 to 2.8 mm zircon silicate balls, bulk density 2.4 kg/L
After filtration and drying, a bright, highly opaque, and fine-particle yellow pigment is obtained. In comparison, the pigment in accordance with Example 4 is as follows (Table 1):
See
The efficacy of the invention is documented primarily by the following incident, highlighted briefly and without any disturbing effects (the pigment is also resistant to leaching), during the development of the product, even though it may seem to be an unorthodox example:
Pilot production began after preliminary results from Examples 1-6 were evaluated. Because of an error in handling, small quantities of very fine nickel antimony rutile yellow pigment traveled out of the mill into the receptacle for the waste water basin (clear side). The pigment was deposited as an extremely well covering, uniform, and intensely luminous lemon yellow coating on the walls and fittings of the waste water preparation system. The “result” looked like it had been applied with a roller or sprayed on in a clean, covering manner. The bright green substrate of the building and the various pipes, fixtures, and cables did not have any more yellow hue nuances in the midday sunlight. The color effect initially led one to think of doped bismuth vanadate or even lead chromate, which could not be disproved without chemical analysis. If one is mindful that all of this occurred without auxiliary agents, the practical value of the improvement from the invention becomes quite clear.
Trial as in Examples 1 and 2A, but, instead of with nickel antimony rutile yellow, with “off-white” titanium dioxide, obtained from a synrutile using the method according to DE-A-101 03 977, which according to the method described therein, but in contrast to Example 3 of DE-A-3 202 158, is obtained directly and does not contain any more “reactive iron”. A batch is produced according to Examples 1 and 2A, but a “synrutile” with 97% TiO2 is used instead of a synthetic mixed phase color pigment. Similarly significant improvements result, in this case with regard to improved brightness, opacity, and gloss, which include the use of a “synrutile” in a direct manner (i.e. without refining methods, using the chloride or sulfate process, that are otherwise usual for TiO2) for pigment applications in the sector of pastel white colors.
In the context of this invention, the qualitative evaluation furthermore leads to the conclusion that the inventive method is applicable to all grain-hard or highly agglomerated pigments that are based on titanium dioxide in a rutile structure, without having to pay for these advantages with weak color for lack of adequate doping, with sharply increased photoactivity, with a significantly increased expenditure of energy and/or non-specific graying due to metal abrasion of the grinding aggregate.
The measured gloss values are determined according to DIN 67 530. An alkyd melamine stoving enamel (55% solid content) was used for the testing system. For this, 80 g resin, 20 g pigment, and 120 g glass beads (2 mm) were weighed into a polypropylene beaker and shaken for 20 minutes on a Scandex shaker. The pigmented resin was applied to a white testing chart (Leneta Form WH) with a wet film thickness of 200 μm using a film drawing device (Erichsen Company, model 509 MCIII) and fired for 30 min at 130° C. Then the reflectometer values were determined with standard illuminant D 65.
Covering power was determined according to DIN 55 97 using standard light D65 (daylight, northern hemisphere, corresponding to emission radiation of the black body heated to 6504 K), using an oxidatively drying alkyd resin. For this, 70 g resin, 30 g pigment, and 120 g glass beads (2 mm) were weighed into a polypropylene beaker and shaken for 20 min on a Scandex shaker. The pigmented resin was applied to black/white contrast cards with wet film thicknesses of 60 to 400 μm using a film drawing device (Erichsen Company, model 509 MCIII) with a type 421/II Erichsen Company step rake. After the resin film was dried, the color spacing DE was determined over black and white substrates according to DIN 6174 and applied graphically against the reciprocal value of the film thickness at which the color spacing is DE=1. This was determined both for the described nickel titanium pigments and for a titanium dioxide pigment for the rutile modification. The covering power in Table II is provided relative to titanium dioxide. The concentration of the tested pigments was less than the critical pigment volume concentration (CPVK).
| Number | Date | Country | Kind |
|---|---|---|---|
| 102004040384.8 | Aug 2004 | DE | national |
This is a U.S. national phase continuation application of PCT application PCT/EP2005/008892 filed Aug. 16, 2005, published Mar. 2, 2006 under WO 2006/021354, and which claims the priority of German Application No. 10 2004 040 384.8, filed Aug. 20, 2004. The prior application is hereby incorporated by reference, in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/EP05/08892 | Aug 2005 | US |
| Child | 11676804 | Feb 2007 | US |
