Preparation of organic additive-treated, pyrogenic silica-encapsulated titanium dioxide particles
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example 1
[0117] Approximately 10 metric tons of pigmentary sized titanium dioxide particles (rutile crystalline phase) substantially encapsulated with about 2.0 wt % pyrogenic silica were produced using commercial scale equipment according to the teaching of U.S. Patent Publication No. 2003 / 0051635. An acidic, aqueous slurry of this material (˜380 g / L) was adjusted to a pH value of ˜8 (sodium hydroxide) and the residual chlorine present in said slurry neutralized. Said slurry was then acidified temporarily to pH 6 (sulfuric acid), subsequently re-adjusted to pH 8.5 (sodium hydroxide) and finally filtered (rotary drum filter). The produced filter cake was removed from the filter apparatus and dropped onto a conveying screw where neat octyltriethoxysilane (OTES) was added to said cake by peristaltic pump. The resulting pigment / OTES mixture was then fed directly to a spray dryer. The resultant dried product (dryer exit temperature ˜100° C.) was then pneumatically conveyed to a fluid energy mill...
example 2
[0118] Approximately 55 metric tons of pigmentary sized titanium dioxide particles (rutile crystalline phase) substantially encapsulated with about 1.5 wt % pyrogenic silica were produced using commercial scale equipment according to the teaching of U.S. patent Publication No. 2003 / 0051635. An acidic, aqueous slurry of this material (˜350 g / L) was adjusted to a pH value of 4.7 (sodium hydroxide) and the residual chlorine present in said slurry neutralized. Said slurry was then filtered using a press plate filter at pH values between 4.0 (pH reductions performed using hydrochloric acid) and 5.1 (pH increases performed using sodium hydroxide). The produced filter cake was conveyed to a flash dryer where said cake was simultaneously dried and treated with varying amounts of neat octyltriethoxysilane (OTES) which was injected directly into the dryer body. The resultant dried product (dryer exit temperature ˜120° C.) was then conveyed to a fluid energy mill (steam micronizer) where it wa...
example 3
[0119] Approximately 194 metric tons of pigmentary sized titanium dioxide particles (rutile crystalline phase) substantially encapsulated with about 2.0 wt % pyrogenic silica were produced using commercial scale equipment according to the teaching of U.S. patent Publication No. 2003 / 0051635. An acidic, aqueous slurry of this material (˜350 g / L) was adjusted to a pH value of 8.0 (sodium hydroxide) and the residual chlorine present in said slurry neutralized. Said slurry was then filtered using a press plate filter at pH values between 4.5 (pH reductions performed using hydrochloric acid) and 8.8 (pH increases performed using sodium hydroxide). The produced filter cake was conveyed to a flash dryer where said cake was simultaneously dried and treated with varying amounts of neat trimethylolpropane (TMP), which was injected directly into the dryer body. The resultant dried product (dryer exit temperature ˜120° C.) was then conveyed to a fluid energy mill (steam micronizer) where it was...
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