Method for making particulate compositions and products thereof
a technology of composition and particulate composition, which is applied in the field of making abrasive compositions, can solve the problems of affecting the appearance of teeth, affecting the quality of teeth, so as to achieve the effect of reducing production costs, reducing production costs, and reducing production costs
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example 1
[0106] A batch of amorphous precipitated silica was prepared in a reactor as follows, which thereafter was subjected to certain dewatering, wet milling and particle classification described below, without any drying or dry milling occurring, to observe the effects of the post-processing procedures that were applied.
[0107] The batch was prepared by adding 502 gallons (1900 L) of sodium silicate (13.0%, 2.50 mole ratio of SiO2:Na2O,) to a reactor and heated it to 85° C. Then sodium silicate (13.0%, 2.50 mole ratio of SiO2:Na2O, preheated to 85° C.) and sulfuric acid (11.4%) were simultaneously added to the reactor at a rate of 102.4 gpm (387.6 L / min) and 45.0 gpm (170.3 L / min). The simultaneous addition of sodium silicate and sulfuric acid continues for 48 minutes, after which time the sodium silicate addition is discontinued. The acid flow was continued until the batch pH dropped to 5.2, at which time the acid flow was stopped. The batch was then digested at 93° C. for 10 minutes, w...
example 2
[0115] A portion of the silica prepared in Example 1 was collected after the reactor, filtered and washed to remove sulfate, then the filter cake was fed at a rate of 0.8 LPM into a 1.5 liter horizontal style media mill (model HML 1.5 Premiere Mill manufactured by Lightnin, Inc., Reading, Pa.) loaded with 1080 ml of 1.6 mm zirconia beads having a specific gravity of 3.7 and set to a speed of 2500 FPM (feet per minute) to reduce the particle size. The silica feed (Example 2A) to the mill had a MPS of 10.8 μm and a distribution span of 4.8. After milling the silica denoted as Example 2B had a MPS of 5.79 μm, a span of 2.31 and was at 34.9% solids. Next, the milled slurry was fed into a 6″ solid bowl continuous flow 6,000 rpm Bird centrifuge (BIRD Machine Company Inc., South Walpole, Mass.) in order to collect a fraction of particles with a MPS of about 6 μm. The silica slurry was fed into the centrifuge at a rate of 8.9 LPM with the centrifuge set to 40 HZ. The overflow was collected ...
example 3
[0120] This batch of amorphous precipitated silica was prepared by adding 474 gallons (1794 L) of sodium silicate (13.30%, 2.65 mole ratio of SiO2:Na2O) to a reactor and heating it to 85° C. Then, simultaneous addition of sodium silicate (13.3%, 2.65 mole ratio of SiO2:Na2O, preheated to 85° C.) at a rate of 92.7 gpm (351 L / min) and sulfuric acid (11.4%) at a rate of 41.5 gpm (157 L / min) was continued for 47 minutes, after which time the sodium silicate addition was discontinued. The acid flow was continued until the batch pH dropped to 5.9±0.1, at which time the acid flow was discontinued. The batch was then digested at 93° C. for 10 minutes, with the pH adjusted back towards 5.9 as needed throughout digestion. After digestion, the pH was manually adjusted to 5.9±0.1, and the batch was discharged from the reactor.
[0121] Example 3 silica had a 5% pH of 7.75, a sodium sulfate content of 0.9%, an oil absorption of 73 ml / 100 g and a median particle size of 27 μm.
[0122] Example 3 sili...
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