Preparation method of spherical silicon dioxide
A spherical silica and carbon dioxide technology, applied in the directions of silica, silica, carbonate preparations, etc., can solve the problems of inability to achieve good application effects, difficult to handle and reuse, and difficult to large-scale industrial production, etc. Achieve the effect of low production cost, large pore volume and narrow particle size distribution
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Embodiment 1
[0035] Spherical silica was prepared as follows:
[0036] (1) Dissolve 6 g of sodium silicate nonahydrate in 100 mL of water, and stir until dissolved at room temperature to obtain an aqueous solution of sodium silicate.
[0037] (2) The sodium silicate aqueous solution obtained in step (1) and pure carbon dioxide gas are simultaneously passed into the membrane dispersion microreactor, and the average pore diameter of the dispersion membrane is 0.5 μm; the volume flow ratio of carbon dioxide gas and sodium silicate aqueous solution is 5:1, The obtained reaction liquid is recycled and fed, and the carbonization reaction temperature is 20° C., and when the pH value of the reaction liquid is 8, the aeration is stopped.
[0038] (3) The reaction solution obtained in step (2) was put into an aging reaction kettle, and aged in a water bath at 80° C. for 10 minutes without stirring during the aging process.
[0039] (4) Centrifuge to obtain a precipitate, wash with water, then dispe...
Embodiment 2
[0042] Spherical silica was prepared as follows:
[0043] (1) Dissolve 6 g of sodium silicate nonahydrate in 300 mL of water, and stir until dissolved at room temperature to obtain an aqueous solution of sodium silicate.
[0044] (2) Pass the sodium silicate aqueous solution obtained in step (1) and pure carbon dioxide gas into the membrane dispersion microreactor simultaneously, and the average pore diameter of the dispersion membrane is 5 μm. The sodium silicate aqueous solution is fed once, the volume flow ratio of carbon dioxide gas and sodium silicate aqueous solution is 2:1, the carbonization reaction temperature is 40°C, and when the pH value of the reaction solution is 8, stop aeration.
[0045] (3) The reaction solution obtained in step (2) was put into an aging reaction kettle, and aged in a water bath at 100° C. for 6 hours without stirring during the aging process.
[0046] (4) Centrifuging and separating to obtain a precipitate, washing with water, then dispersin...
Embodiment 3
[0049] Spherical silica was prepared as follows:
[0050] (1) Dissolve 6 g of sodium silicate nonahydrate in 100 mL of water, and stir until dissolved at room temperature to obtain an aqueous solution of sodium silicate.
[0051] (2) Pass the sodium silicate aqueous solution obtained in step (1) and mixed gas (50% carbon dioxide+50% nitrogen) into the membrane dispersion microreactor simultaneously, and the average pore size of the dispersion membrane is 50 μm. The obtained reaction liquid is recycled and fed, the volume flow ratio of the mixed gas to the sodium silicate aqueous solution is 10:1, the carbonization reaction temperature is 15°C, and when the pH value of the reaction liquid is 8, the aeration is stopped.
[0052] (3) The reaction solution obtained in step (2) was put into an aging reaction kettle, and aged in a water bath at 85° C. for 10 minutes, and the stirring speed was 500 rpm during the aging process.
[0053] (4) Centrifuging and separating to obtain a prec...
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