Dispersion of high surface area silica
A dispersion, surface area technology, applied in the direction of silica, silicon oxide, nanotechnology for materials and surface science, which can solve the problem of low cost
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Embodiment P1
[0046] Potassium-silicon mixed oxide powder P1 (according to German patent application: patent application number 102005027720.9, application date June 16, 2005): evaporate 85kg / h of SiCl 4 , and transfer it to the center tube of a burner of the type described in DE-A-19650500. Additionally, feed 40m into the pipe 3 / h(stp) of hydrogen and 124m 3 / h(stp) of air. The gas mixture exits the inner burner nozzle and burns in the combustion chamber of the water-cooled flame tube. In order to avoid caking situation, feed another 4m 3 / h(stp) of secondary hydrogen into the jacketed nozzle surrounding the central nozzle.
[0047] The aerosol is obtained from a 5% strength potassium chloride aqueous solution through a two-fluid nozzle mounted on the base of the container. Produce 1100g / h aerosol. With the help of 18m 3 / h(stp) carrier gas (air) flow, carrying the aerosol through an externally heated tube, directs the carrier gas so that it first impinges laterally on the tray bas...
Embodiment P2
[0050] Potassium-silicon mixed oxide powder P2 (according to European Patent Application: Patent Application No. 05024753.5, filing date 12.11.2005): evaporated 4.44 kg / h of SiCl 4 . With the help of 3.3m 3 / h(stp) of air is used as carrier gas to transfer the vapors into the mixing chamber. In addition, the 2.3m 3 / h(stp) of core hydrogen and 6.9m 3 / h(stp) of primary air is introduced into the mixing chamber. In the central tube, the reaction mixture is fed to a burner and ignited. The flame burns in a water-cooled combustion tube. Bring in another 20m 3 / h(stp) secondary air to the reaction chamber. At a temperature of 320° C., 191 g / h of a 3.0% by weight aqueous solution of potassium chloride were introduced through nozzles into the flow of silica granules, hydrochloric acid, air and nitrogen. After an average residence time of 12 ms, the temperature of the mixture was raised to 500°C. After an average residence time of 24 s, metal oxide particles were deposited i...
Embodiment D1
[0054] A 100 liter stainless steel batch vessel was charged with 45.0 kg of DI (fully demineralized) water. Then, 30 kg of P1 was sucked in under shear conditions using the suction tube of Ystral Conti-TDS 3 (stator slot: 4 mm ring and 1 mm ring, rotor / stator distance: about 1 mm). After the addition was complete, the suction port was closed, followed by shearing at 3000 rpm for 20 minutes. The heat generated during dispersion operation is removed by an external heat exchanger. Using 20 kg of DI water, the dispersion was diluted and the pH was adjusted from 3.4 to 10.0 with 2.6 kg of aqueous potassium hydroxide (30% strength) under shear. Then, 2.4 kg DI water was added to obtain 30 wt% SiO 2 Content, repeated shearing for about 5 minutes to homogenize.
[0055] The average aggregate diameter was 81 nm (measured with Horiba LA 910) or 47 nm (measured with Zetasizer 2000HS, Malvern).
[0056] Even after 6 months, the dispersion showed no signs of gelling or settling.
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Abstract
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