Stable aqueous colloidal silica product, and methods to make and use same
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example 1
[0067]Preparation of a Colloidal Silica Sol of the Invention. Inventive aqueous colloidal silica products (Samples 7-15 in Table 1) were prepared using the lab-scale semi-batch procedure described as follows. Charge a reaction vessel with 600 mL of Amberlite® IRC84SP ion exchange resin (available from Dow) in its sodium form. Following manufacturer's procedure for regenerating the resin to the hydrogen form such that the regeneration is at least 40 percent complete. Rinse the resin clean with water and drain the water. Charge 190-380 grams of water into the vessel and start mixing the contents of the vessel to suspend the resin. Next, heat the contents of the reactor to 100-160 degrees F. Charge the reaction vessel (over a period of about 2-20 minutes) with 186-505 grams of sodium silicate (having a mole ratio of SiO2 to Na2O of 3.26 and a pH of 11.2). After 1-45 min, charge the reaction vessel (over a period of about 5-30 minutes) with 13-160 grams of sodium silicate. Stir the cont...
example 2
[0070]For Example 2, inventive aqueous colloidal silica products (Samples 16-29 in Table 2) were prepared using the following pilot-scale semi-batch procedure. Charge a reaction vessel with 185 gallons of Amberlite® IRC84SP ion exchange resin (available from Dow) in its sodium form. Following manufacturer's procedure for regenerating the resin to the hydrogen form such that the regeneration is at least 40 percent complete. Rinse the resin clean with water and drain the water. Charge 683-1158 lbs of water into the vessel and start mixing the contents of the vessel to suspend the resin. Next, heat the contents of the reactor to 100-160 degrees F. Charge the reaction vessel (over a period of about 2-20 minutes) with 574-1320 lbs of sodium silicate (having a mole ratio of SiO2 to Na2O of 3.26 and a pH of 11.2). After 1-45 min, charge the reaction vessel (over a period of about 5-30 minutes) with 41-417 lbs of sodium silicate. Stir the contents in the reaction vessel for another 10-180 m...
example 3
[0072]A control sample and Samples 17-19 of Example 2 were utilized in comparison experiments related to first pass ash retention of each. Each of the samples were dosed onto a cellulosic furnish.
[0073]As can be seen, a 90% first pass ash retention can be achieved using approximately 0.5 to 0.8 as much microparticle dosage (FPAR replacement ratio) for each of Samples 17-19, as compared to the control sample. These results are graphically demonstrated in FIG. 1.
MicroparticleFirst Pass Ash Retention (%)Dosage, lbSampleSample Samplemicroparicles / tonControl171819073.573.573.573.50.2579.276.376.779.10.580.582.783.084.0185.590.488.290.41.589.395.194.994.6292.294.894.996.9
[0074]As can be seen, the inventive aqueous colloidal silica products prepared using the inventive production method provided superior results compared to the control sample.
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