Titanium dioxide slurries
View Patent ↗Improved methods for producing titanium dioxide slurries. The output from a micronizer is passed through a condenser to condense the steam and form an aqueous slurry of titanium dioxide, which can in most cases then be further concentrated as desired or which can be sold or used without further concentration, instead of passing the micronizer output to apparatus for separating the TiO2 from the steam, as is currently practiced in the art. The resultant slurry from the condenser is in a further refinement preferably sent to an agitated storage tank together with dispersant and anti-settling compounds to aid in preventing settling of the titanium dioxide solids out of the slurry. To help facilitate condensation of the steam/pigment mixture sent to the condenser, a portion of the condensed slurry is in yet a further refinement pumped from the slurry storage tank to a heat exchanger. The output from the heat exchanger is then fed to the condenser to facilitate the condensing of the steam in the condenser. The temperature and volume (flow) of cooled condensate to the condenser are set to match the amount of steam and its temperature so as to ensure that substantially all of the steam and contained pigment are collected from the condenser.
1. An apparatus for producing a titanium dioxide slurry, comprising:
a micronizer that produces an output comprising titanium dioxide and steam;
a condenser that receives the micronizer output and combines the micronizer output with a first titanium dioxide slurry to condense the titanium dioxide and steam mixture and produces a resulting titanium dioxide slurry.
2. An apparatus for producing a titanium dioxide slurry, comprising:
a micronizer that produces an output comprising titanium dioxide and steam;
a condenser that receives the micronizer output and combines the micronizer output with a first titanium dioxide slurry to condense the titanium dioxide and steam mixture and produces a resulting titanium dioxide slurry;
a storage tank that receives the resulting titanium dioxide slurry and recycles some of the resulting titanium dioxide slurry to the condenser.
3. An apparatus according to claim 1 , wherein the micronizer produces an output comprises from about 25 percent to about 50 percent titanium dioxide.
4. An apparatus according to claim 1 , wherein the temperature of the micronizer output is at least about 300° F.
5. An apparatus according to claim 1 , wherein the temperature of the micronizer output is at least about 400° F.
6. An apparatus according to claim 1 , wherein the temperature of the micronizer output is not more than about 600° F.
7. An apparatus according to claim 1 , wherein the temperature of the micronizer output is no more than about 500° F.
8. An apparatus according to claim 1 , wherein the resulting slurry comprises at least about 40 percent by weight of titanium dioxide.
9. An apparatus according to claim 2 , wherein the temperature of the first titanium dioxide slurry is lower than the temperature of the micronizer output.
10. An apparatus according to claim 2 , wherein the micronizer output and the first titanium dioxide slurry comprise approximately the same percentage by weight of titanium dioxide.