Preparation method and application of pearlescent pigment

Abstract

The present invention relates to a method for preparing pearlescent pigment through metal oxide coating based on a sheet-like substrate, and the obtained pearlescent pigment. The present invention further relates to a method for preparing pearlescent pigment through coating a sheet-like substrate by hydrolyzing metal salt under an acid condition, wherein a pH value is adjusted by using inorganics such as MgO, MgOH or CaCO.sub.3 that does not dissolve in water but can dissolve through reacting with an acid. According to the method, no free metal oxide is generated when the metal salt is hydrolyzed, so that the production cost is reduced, product quality is improved, problems possibly generated in an application process of the product are avoided, and a production process is more environment-friendly.

Claims

1. A method for preparing pearlescent pigment, comprising: A) in the presence of sheet-like substrates and at a set pH value which allows metal salt for coating to be hydrolyzed, performing hydrolysis coating by adding the metal salt for coating and inorganics simultaneously into water, wherein the inorganics does not dissolve in water but can dissolve through reacting with an acid, and the inorganics is used to adjust or maintain a pH value of a hydrolysis system, wherein relative to 1000 parts by weight of the sheet-like substrates, 450-1350 parts by weight of the metal salt and 400-1200 parts by weight of the inorganics are used.

2. The method according to claim 1, wherein the set pH value is within a range of 0.5-3.

3. The method according to claim 1, wherein the inorganics that does not dissolve in water but can dissolve through reacting with an acid is alkaline-earth metal compound.

4. The method according to claim 1, wherein the method further comprises the following steps of: B) filtering, C) washing, D) drying and E) calcining.

5. The method according to claim 1, wherein the metal salt for coating is added in a form of a water solution; and/or, the inorganics that does not dissolve in water but can dissolve through reacting with the acid is added in a slurry form formed in water; and/or the adding rate of the inorganics that does not dissolve in water but can dissolve through reacting with the acid is controlled in the step A) so that the pH value of the hydrolysis system is kept stable.

6. The method according to claim 1, wherein the sheet-like substrates is selected from one or two or more of natural mica, synthetic mica, glass sheet, sheet-like aluminum oxide and sheet metal; and/or the metal salt for coating is selected from one or two or more of TiCl.sub.4, TiOCl.sub.2, FeCl.sub.3 or SnCl.sub.4; and/or the inorganics is selected from magnesium oxide, magnesium hydroxide, calcium carbonate or a mixture thereof.

7. The method according to claim 3, wherein after calcined, the metal salt for coating becomes one of the following components: anatase TiO.sub.2, SnO.sub.2, rutile TiO.sub.2, Fe.sub.2O.sub.3, TiO.sub.2+FeO.sub.3, SnO.sub.2+TiO.sub.2+Fe.sub.2O.sub.3, SnO.sub.2+Fe.sub.2O.sub.3, Ti and Fe mixed oxide and Sn, Ti and Fe mixed oxide.

8. The pearlescent pigment obtained by using the method according to claim 1.

9. Use of the pearlescent pigment according to claim 8 in the field of paints, printing ink, plastics, ceramic materials, leather coloration, wallpaper, powder coating or cosmetics.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a situation where hydrolysis coating slurry samples prepared by a new process (left) of the present invention and that by a conventional process (right) are respectively placed in glass bottles after a certain time of resting and sedimentation.

DETAILED DESCRIPTION OF THE INVENTION

(2) The following examples are used to make detailed description of, rather than limitation on, the present invention.

EXAMPLE 1

(3) 1000 kg natural mica substrates with particle diameters D.sub.10=10 m, D.sub.50=25 m, D.sub.90=60 m are added to 10000 L deionized water (the reaction kettle is 20000 L), stirred and heated to 80 C., adjusting to pH value of 1.0 by using 1:1 hydrochloric acid. MgO slurry is prepared: 1000 kg 99% MgO is added to 5000 L water and stirred to prepare a slurry with total solid concentration of 20%. A particle diameter of less than 200 mesh is chosen to prevent the prepared slurry from sedimentation. At the start of hydrolysis coating, a titanium solution pump and an MgO slurry pump are operated simultaneously, and the pH value is automatically controlled to 1.0 by using a pH meter. A titanium solution is formulated with TiCl.sub.4 having purity of not less than 99% and water with a proportion of water to TiCl.sub.4 of 1:1 to prepare a titanium tetrachloride solution with the concentration of 2 mol/L, which may generate HCl gas when diluting. The released HCl gas is absorbed with water to obtain hydrochloric acid. Enough hydrochloric acid is added to prevent the diluted TiCl.sub.4 from hydrolytic spoilage. The pH value is constantly 1.0 by simultaneously pumping the titanium solution and MgO slurry to the reaction kettle. The added titanium solution constantly forms a coating on the mica substrates by hydrolysis, when the pH value is 1.0. After filtering, washing and calcining, pearlescent products having silvery white, iridescence and the like are obtained. The amount of the TiCl.sub.4 solution determines the color of the final product to be golden yellow, orange, red, purple, blue, green and so on.

(4) TABLE-US-00001 Titanium solution MgO slurry with with the total solid TiO.sub.2 coating Color of Mica, concentration of concentration of thickness, product kg 2 mol/L, liter 20%, liter nm Silvery white 1000 1800 (TiCl.sub.4 with 2000 (MgO, 45 the purity of not 400 kg) less than 99%, 450 kg) Golden 1000 2800 3100 70 yellow Red 1000 3800 4200 95 Blue 1000 4600 5100 115 Green 1000 5400 (99% TiCl.sub.4, 6000 (MgO, 135 1350 kg) 1200 kg)

(5) Compared with a conventional process (controlling pH value of the hydrolyzed coating with a base solution such as sodium hydroxide), the present invention provides a notable improvement in both lightness and chromaticity of products obtained through the new process thereof, and water consumption is saved by more than a half when filtering and watering. All these indicate that no free particles are generated in the new process when hydrolyzing; therefore, it is easier to filter and wash, and the product has better quality.

(6) Another method showing that no free particles are generated in the products obtained by using the new process comprises: respectively placing hydrolyzed coatings obtained by using the new process and conventional process in glass bottles. An upper mother solution (left) of the hydrolyzed coating slurry samples prepared by using the new process is more transparent than that of the conventional process after a certain time of standing and sedimentation (see FIG. 1). It can be seen from FIG. 1 that a mother solution in the upper layer in dispersion of the present invention is transparent while a mother solution in the upper layer in dispersion of the prior art is hazy.

(7) A method of evaluating sample quality by adopting a common coating swipe card or jet plate comprises: adding a proper amount of pearlescent powder samples (10%) to resin or paint, and forming coating through the coating swipe card or jet plate, and drying. Data of color and finish degree is measured with an X-Rite MA68 color difference meter. Data is shown by using a CIE L*, a*, b* system. L* indicates brightness, c value (c.sup.2=a.sup.2+b.sup.2) indicates color concentration.

EXAMPLE 2

(8) Mica slurry, titanium solution and MgO slurry are prepared according to example 1, and a 20% SnCl.sub.4 solution is prepared. 10 kg SnCl.sub.4 is dissolved in 40 kg deionized water and pumped into a reaction kettle with a PH value of 1.0, then coated with titanium according to example 1, and the pH value is automatically controlled at 1.0 with MgO slurry. After a desired color is obtained, filtering, washing, drying and calcining are conducted to obtain a product. Taking a silver white product as examples, the weights of mica, 99% TiCl.sub.4, SnCl.sub.4 and MgO are respectively 1000:450:10:400 (kg). The thickness of the coating is about 45 nm.

(9) The obtained product is pearlescent powder without free TiO.sub.2.

EXAMPLE 3

(10) As described in example 1, mica slurry and MgO slurry are prepared and pH value is adjusted to 3.0. A 10% FeCl.sub.3 solution is prepared by dissolving 1000 kg FeCl.sub.3 in 9000 L deionized water. a FeCl.sub.3 solution and MgO slurry are simultaneously pumped and pH value is automatically controlled at 3.0. Pearlescent powder with metallic lustre can be obtained through filtering, washing and calcining after adding a proper amount of FeCl.sub.3 solution to the reaction kettle. The amount of the FeCl.sub.3 solution determines a color of the final product to be golden, orange, red, purple, blue, green and so on. Taking a brass golden product as an example, the amounts of mica, MgO and FeCl.sub.3 by dry weight are respectively 1000:400:400 (kg). The thickness of the final coating is about 50 nm.

EXAMPLE 4

(11) Mica slurry is prepared, and coated with SnO.sub.2 according to example 2. With pH value adjusted to 3.0, iron coating is conducted according to example 3. Pearlescent powder with metallic lustre is obtained through filtering, washing and calcining. The amount of the FeCl.sub.3 solution determines the color of the final product to be golden, orange, red, purple, blue, green and so on. Taking a brass golden product as an example, the actual amounts of mica, ferric trichloride (not titanium tetrachloride) and MgO and SnCl.sub.4 are 1000:400:400:10 (kg). The thickness of the final coating is about 50 nm.

EXAMPLE 5

(12) Titanium coating is performed according to example 1, and then iron coating is performed according to example 3 with pH value adjusted to 3.0. Pearlescent powder with two-layer coatings of titanium and iron with metallic lustre can be obtained through filtering, washing and calcining. The color of the final product is determined with the proportion and amount of titanium and iron.

EXAMPLE 6

(13) Titanium coating is performed according to example 2 and then iron coating is performed according to example 3 to produce pearlescent pigment with 2 layers of titanium and iron.

EXAMPLE 7

(14) A Ti liquid in example 1 and molten iron in example 3 are mixed according to the weight ratio of 100:10(Ti:Fe), mica slurry is prepared according to example 1, a PH value is adjusted to 2.5, and the pH value is automatically controlled at 2.5 by using MgO slurry so as to perform TiFe mixed coating.

EXAMPLE 8

(15) Tin coating is performed according to example 2, and then, TiFe mixed coating is performed according to example 7.

EXAMPLE 9

(16) The coating processes in examples 1-8 are repeated except that synthetic mica is used as the sheet-like substrates.

EXAMPLE 10

(17) Example 9 is repeated except that glass sheets are used as the sheet-like substrates.

EXAMPLE 11

(18) Example 9 is repeated except that aluminum oxide is used as the sheet-like substrates.

EXAMPLE 12

(19) Example 9 is repeated except that metal sheets made of Al, Cu, Ni and various alloys are used as the sheet-like substrates.

EXAMPLE 13

(20) Examples 1-12 are repeated except that the pH control agent MgO slurry is changed into Mg(OH).sub.2 slurry or a mixture of MgO slurry and Mg(OH).sub.2 slurry.

EXAMPLE 14

(21) Example 13 is repeated except that the pH control agent is calcium carbonate (CaCO.sub.3) slurry or a mixture of CaCO.sub.3/MgO/Mg(OH).sub.2 at any ratio.

APPLICATION EXAMPLES

(22) The pearlescent pigment prepared according to examples 1-14 is applied to the fields such as paints, coatings, printing ink, plastics, ceramic materials, leather coloration, wallpaper, powder coatings and cosmetics. For example, a coating with excellent color and luster can be prepared if the pearlescent pigment of the present invention is added to a paint or coating.

Application Example 1: Using Paint Spraying as an Example

(23) 4.0 g of the pearlescent pigment is accurately weighed, 4.0 g of butyl acetate and 8.0 g of polyester automobile coating resin are added, dispersed for 10 min after stirring in a stirrer, and 84.0 g of automobile coating resin systems are further added, and stirred for 5 min. The viscosity of the coating is regulated to Ford 4# cup for 14-15 s before spraying. A temperature of a spraying chamber is controlled at 25 C. and a relative humidity at 60% during spraying. With twice spray, a varnish is covered after flash drying for 10 min, and baked at 140 C. for 30 min after performing flash drying again.

Application Example 2: Using Injection Molding as an Example

(24) 200 g of polypropylene (PP) materials are accurately weighed and dried at 105 C., put into a sealed plastic bag, added with 1 ml of gloss oil (or dispersed oil), then, shaken to sufficiently mix the gloss oil and the polypropylene materials. 4.000 g of the pearlescent powder is accurately weighed by using an analytical balance, put into the sealed plastic bag, shaken again, and rubbed to sufficiently evenly disperse the pearlescent powder into PP particles.

(25) After a temperature of a charging barrel reaches a set value (generally 180-200 C.), the prepared polypropylene materials are added into a hopper, and original remained materials in the charging barrel are extruded by virtue of rubber injection and rubber melting functions until new materials are extruded, wherein the extruded new materials need to have luster without impurities, dark spots, scorch or air bubbles, and meanwhile, nozzles are required to have no blocking phenomenon during rubber injection. Produced plastic sheets are stable and qualified products and automatic normal production can be carried out after front and back produced plastic sheets have no difference.