Preparation method of ultra-high-purity silicon tetrachloride
A pure silicon tetrachloride, silicon tetrachloride technology, applied in chemical instruments and methods, halide silicon compounds, inorganic chemistry and other directions, can solve the problem of difficult to remove hydrogen impurities
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[0022] According to a typical embodiment of the present invention, a method for preparing ultra-high-purity silicon tetrachloride is provided. The method comprises the following steps: S1, continuously feeding high-purity silicon tetrachloride into the photochemical reactor under the action of nitrogen; S2, continuously feeding chlorine gas into the photochemical reactor under the condition of ultraviolet light to make the high-purity silicon tetrachloride The hydrogen-containing impurities in the silicon dioxide react with chlorine to obtain the primary product; S3, the primary product is passed into the stripping tower from the upper part of the stripping tower, and the nitrogen gas is fed from the bottom of the stripping tower to remove the primary product. The unreacted chlorine in the product is obtained as a secondary product; and S4, the secondary product is sent to a silicon tetrachloride purification tower, and after continuous light removal and weight removal, ultra-h...
Embodiment 1
[0042] Such as figure 1 As shown, the ultra-high-purity silicon tetrachloride production process of the present embodiment comprises the following steps:
[0043] S1, the purity is more than 99.9999%, that is, high-purity silicon tetrachloride raw material, which contains trace impurities such as trichlorosilane, methylchlorosilane and borophosphorus, and uses high-purity nitrogen to send the raw material silicon tetrachloride into the photochemical reaction device , the dew point of the high-purity nitrogen is not lower than -90°C.
[0044]S2, after sending the high-purity silicon tetrachloride raw material into the photochemical reaction device, under the condition of ultraviolet light, a certain amount of high-purity chlorine gas is passed into the photochemical reactor. In this method, the liquid material of high-purity silicon tetrachloride is fed first, and then the gas material of high-purity chlorine is fed. Among them, the photochemical reactor is composed of a micr...
Embodiment 2
[0060] Processing step is with embodiment 1, and concrete condition is as follows:
[0061] The purity of the raw material silicon tetrachloride is above 99.9999%, and the silicon tetrachloride after polysilicon reduction tail gas and hydrogenation condensate purification can meet the requirements. The dew point temperature of high-purity nitrogen is not lower than -90°C, and the purity of high-purity chlorine is not lower than 99.999%.
[0062] The photochemical reactor is a quartz microchannel reaction device, the diameter of the reaction channel is micron, the reaction temperature is 20°C, the reaction pressure is 0.3MPa, the volume ratio of high-purity chlorine gas and raw material silicon tetrachloride is 1:1, and the light source can use high pressure UV mercury lamp or cold light source UV lamp. The heat exchange medium is heat conduction oil, which is used to cool the photochemical reaction device and maintain the reaction temperature in the reactor.
[0063] The pro...
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