Making co-precipitated mixed oxide-treated titanium dioxide pigments
View Patent ↗Simplified and improved processes are provided for manufacturing titanium dioxide pigments including a surface treatment whereby a plurality of inorganic oxides or a combination of one or more inorganic oxides with one or more inorganic phosphates are applied to a titanium dioxide base pigment. Aqueous acid-soluble sources of the desired inorganic oxides and/or phosphates are predissolved in an aqueous acid, and these can be added on a batch wise or more preferably on a continuous basis to an alkaline slurry containing the titanium dioxide base pigment and to which aqueous alkaline-soluble sources of the desired inorganic oxides are being or have been added previously. Co-precipitation of the oxides and/or oxides and phosphates is then accomplished by an adjustment of the pH, to provide a surface treated pigment with excellent homogeneity of the deposited mixed oxides and/or oxides and phosphates.
1. A process for manufacturing a titanium dioxide pigment, comprising the steps of:
a) preparing an aqueous alkaline slurry of a titanium dioxide base pigment, said titanium dioxide base pigment being produced by a sulfate process or a chloride process for producing titanium dioxide pigment;
b) adding to said aqueous alkaline slurry of titanium dioxide base pigment at least one aqueous alkali-soluble source of an inorganic oxide;
c) dissolving at least one aqueous acid-soluble source of an inorganic oxide and/or at least one aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate into an aqueous sulfuric acid solution containing from about 5 percent by weight to about 98 percent of sulfuric acid;
d) following step c), co-precipitating a uniform mixture of inorganic oxides and/or phosphates on said titanium dioxide base pigment by gradually adding said sulfuric acid solution to said aqueous alkaline slurry of titanium dioxide base pigment, said sulfuric acid solution being added to said aqueous alkaline slurry of titanium dioxide base pigment in an amount sufficient to achieve a final slurry pH value between about 4 and about 8.5 whereby the co-precipitation of the aqueous acid-soluble source of inorganic oxide and/or the aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate occurs upon precipitation of the aqueous alkali-soluble source of an inorganic oxide.
2. A process according to claim 1 , wherein the titanium dioxide base pigment selected has previously been surface treated to deposit at least one inorganic oxide thereon from the group consisting of the inorganic oxides of aluminum, boron, phosphorus, silicon, titanium and zirconium.
3. A process according to claim 2 , wherein the titanium dioxide base pigment used to form the aqueous alkaline slurry includes from about 0.5 percent to about 5 percent by weight of the inorganic oxide or oxides, based on the weight of the treated pigment as a whole.
4. A process according to claim 1 , wherein the at least one aqueous alkali-soluble source of an inorganic oxide added in step b) to the slurry of step a) is selected from the group consisting of the aqueous alkali-soluble oxide salts of aluminum, boron, phosphorus and silicon.
5. A process according to claim 4 , wherein sodium or potassium salts of aluminum, boron, phosphorus or silicon are used and added in the form of an aqueous solution containing from about 1 percent to about 50 percent by weight of the dissolved salts.
6. A process according to claim 5 , wherein sodium or potassium salts of aluminum, boron, phosphorus or silicon are used and added in the form of an aqueous solution containing from about 5 percent to about 40 percent by weight of the dissolved salts.
7. A process according to claim 6 , wherein sodium or potassium salts of aluminum, boron, phosphorus or silicon are used and added in the form of an aqueous solution containing from about 15 percent to about 35 percent by weight of the dissolved salts.
8. A process according to claim 1 , wherein the at least one aqueous acid-soluble source of an inorganic oxide or of a cation capable of forming a water-insoluble phosphate is selected from the group consisting of the aqueous acid-soluble salts of aluminum, cerium, tin, titanium and zirconium.
9. A process according to claim 8 , wherein the at least one aqueous acid-soluble source of an inorganic oxide or of a cation capable of forming a water-insoluble phosphate is added and dissolved into the aqueous sulfuric acid solution in the form either of a previously prepared aqueous metal salt solution or in solid salt form.
10. A process according to claim 1 , wherein the aqueous sulfuric acid solution used in step c) contains from about 20 percent by weight to about 50 percent by weight sulfuric acid.
11. A process according to claim 10 , wherein the aqueous sulfuric acid solution used in step c) contains from about 25 percent by weight to about 40 percent by weight sulfuric acid.
12. A process according to claim 1 , wherein the titanium dioxide base pigment is from about 5 percent to about 65 percent by weight of the aqueous alkaline slurry.
13. A process according to claim 12 , wherein the titanium dioxide base pigment is from about 15 percent to about 45 percent by weight of the aqueous alkaline slurry.
14. A process according to claim 13 , wherein the titanium dioxide base pigment is from about 25 percent to about 40 percent by weight of the aqueous alkaline slurry.
15. A process according to claim 1 , wherein the uniform mixture of inorganic oxides and/or phosphates that are co-precipitated from the alkali-soluble and acid-soluble sources collectively comprise from about 0.2 percent to about 10 percent by weight of the titanium dioxide base pigment.
16. A process according to claim 15 , wherein the uniform mixture of inorganic oxides and/or phosphates that are co-precipitated from the alkali-soluble and acid-soluble sources collectively comprise from about 0.5 percent to about 8 percent by weight of the titanium dioxide base pigment.
17. A process according to claim 16 , wherein the uniform mixture of inorganic oxides and/or phosphates that are co-precipitated from the alkali-soluble and acid-soluble sources collectively comprise from about 1.0 percent to about 5 percent by weight of the titanium dioxide base pigment.
18. A process according to claim 15 , wherein the weight ratio of co-precipitated oxide(s) and/or phosphate(s) from the alkali-soluble sources to the acid soluble sources thereof is from about 30:1 to about 1:10.
19. A process according to claim 18 , wherein the weight ratio of co-precipitated oxide(s) and/or phosphate(s) from the alkali-soluble sources to the acid soluble sources thereof is from about 20:1 to about 1:1.
20. A process according to claim 19 , wherein the weight ratio of co-precipitated oxide(s) and/or phosphate(s) from the alkali-soluble sources to the acid soluble sources thereof is from about 15:1 to about 2:1.
21. A process according to claim 1 , further comprising depositing a wet treatment aluminum oxide onto the titanium dioxide base pigment, while maintaining a slurry pH between about 4 to about 8.5, after substantially completely co-precipitating the mixed inorganic oxides and/or inorganic oxide and phosphate combination onto the pigment according to step d).
22. A process for manufacturing a titanium dioxide pigment, comprising the steps of:
a) dissolving at least one aqueous acid-soluble source of an inorganic oxide and/or at least one aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate into an aqueous sulfuric acid solution;
b) dissolving at least one alkali-soluble source of an inorganic oxide into an aqueous alkaline solution;
c) forming an aqueous alkaline slurry of a titanium dioxide base pigment, said titanium dioxide base pigment being produced from a sulfate process or a chloride process for producing titanium dioxide;
d) after step c), co-precipitating a uniform mixture of inorganic oxides and/or phosphates on said titanium dioxide base pigment by gradually adding both said sulfuric acid solution and said aqueous alkaline solution to said aqueous alkaline slurry of titanium dioxide base pigment, said sulfuric acid and aqueous alkaline solutions being added to said aqueous alkaline slurry of titanium dioxide base pigment in amounts sufficient to achieve a final slurry pH value between about 4 and about 8.5 whereby the co-precipitation of the aqueous acid-soluble source of inorganic oxide and/or the aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate occurs upon precipitation of the alkali-soluble source of an inorganic oxide.
23. A process for manufacturing a titanium dioxide pigment, comprising the steps of:
a) preparing an aqueous alkaline slurry of a titanium dioxide base pigment, said titanium dioxide base pigment being produced by a sulfate process or a chloride process for producing titanium dioxide pigment;
b) adding to said aqueous alkaline slurry of titanium dioxide base pigment at least one aqueous alkali-soluble source of an inorganic oxide;
c) dissolving at least one aqueous acid-soluble source of an inorganic oxide and/or at least one aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate into an aqueous acid solution containing from about 5 percent by weight to about 98 percent of an aqueous acid;
d) following step c), co-precipitating a uniform mixture of inorganic oxides and/or phosphates on said titanium dioxide base pigment by gradually adding said aqueous acid solution to said aqueous alkaline slurry of titanium dioxide base pigment, said aqueous acid solution being added to said aqueous alkaline slurry of titanium dioxide base pigment in an amount sufficient to achieve a final slurry pH value between about 4 and about 8.5 whereby the co-precipitation of the aqueous acid-soluble source of inorganic oxide and/or the aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate occurs upon precipitation of the aqueous alkali-soluble source of an inorganic oxide.
24. A process for manufacturing a titanium dioxide pigment, comprising the steps of:
a) dissolving at least one aqueous acid-soluble source of an inorganic oxide and/or at least one aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate into an aqueous acid solution;
b) dissolving at least one alkali-soluble source of an inorganic oxide into an aqueous alkaline solution;
c) forming an aqueous alkaline slurry of a titanium dioxide base pigment, said titanium dioxide base pigment being produced from a sulfate process or a chloride process for producing titanium dioxide;
d) after step c), co-precipitating a uniform mixture of inorganic oxides and/or phosphates on said titanium dioxide base pigment by gradually adding both said aqueous acid solution and said aqueous alkaline solution to said aqueous alkaline slurry of titanium dioxide base pigment, said aqueous acid and aqueous alkaline solutions being added to said aqueous alkaline slurry of titanium dioxide base pigment in amounts sufficient to achieve a final slurry pH value between about 4 and about 8.5 whereby the co-precipitation of the aqueous acid-soluble source of inorganic oxide and/or the aqueous acid-soluble salt of a cation capable of forming a water-insoluble phosphate occurs upon precipitation of the alkali-soluble source of an inorganic oxide.