Preparation method of submicron spherical silica powder
A spherical silica, sub-micron technology, applied in the direction of silica, silicon oxide, etc., can solve the problems of product purity decline, unsuitable for large-scale production, high equipment requirements, and achieve good filling and fluidity, The preparation process is safe and environmentally friendly, and the preparation method is simple.
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Embodiment 1
[0016] Example 1, a preparation method of submicron spherical silica powder, the steps are as follows:
[0017] (1) Raw material: select silica powder as raw material, the specific surface area of the raw material = 6.8 m 2 / g, the ratio of D90 to D10 is 3.6;
[0018] (2) Preparation: Use oxygen as the carrier gas, liquefied natural gas as combustible gas, and oxygen as the combustion aid. The liquefied natural gas and oxygen are separately introduced into the burner and ignited. The temperature of the flame in the burner is greater than 1800°C, and the raw material is in the carrier gas. It enters into the combustion furnace under protection and spheroidizes to obtain spherical silica powder with average particle size D50=1.8μm; the flow of combustible gas is 250Nm 3 / h, the flow of combustion-supporting agent is 500 Nm 3 / h, the carrier gas flow rate is 150 Nm 3 / h, the feeding frequency is 50Hz.
Embodiment 2
[0019] Embodiment 2, a method for preparing submicron spherical silica powder, the steps are as follows:
[0020] (1) Raw material: select silica powder as the raw material, the specific surface area of the raw material = 10.5m 2 / g, the ratio of D90 to D10 is 11.0;
[0021] (2) Preparation: Use oxygen as the carrier gas, liquefied natural gas as combustible gas, and oxygen as the combustion promoter. The liquefied natural gas and oxygen are respectively introduced into the combustion furnace and ignited. The raw materials enter the combustion furnace under the protection of the carrier gas. The temperature of the flame is greater than 1800°C, spheroidization, that is, spherical silica powder with an average particle size D50=0.6μm is obtained; the flow of combustible gas is 90Nm 3 / h, the flow of combustion-supporting agent is 180Nm 3 / h, the carrier gas flow rate is 180 Nm 3 / h, the feeding frequency is 30Hz.
Embodiment 3
[0022] Example 3, a method for preparing submicron spherical silica powder, the steps are as follows:
[0023] (1) Raw material: select silicon nitride powder as the raw material, the specific surface area of the raw material =9.8m 2 / g, the ratio of D90 to D10 is 3.0;
[0024] (2) Preparation: Air is used as carrier gas, LNG is used as combustible gas, and oxygen is used as combustion aid. Liquefied natural gas and oxygen are separately introduced into the combustion furnace and ignited. The temperature of the flame in the combustion furnace is greater than 1800°C, and the raw materials are in the carrier gas. It enters the combustion furnace under protection and spheroidizes to obtain spherical silica powder with an average particle size of D50=0.4μm; the flow of combustible gas is 120Nm 3 / h, the flow of combustion-supporting agent is 240 Nm 3 / h, the carrier gas flow is 130 Nm 3 / h, the feeding frequency is 60Hz.
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Abstract
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