A method and device for producing chlorosilanes using organic silicon slag
A chlorosilane and organosilicon technology, applied in the field of chlorosilane production, can solve the problems of high impurity content, small particle size of silicon slag, and difficult reaction control.
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Embodiment 1
[0082] This embodiment provides a method for producing chlorosilanes using organic silicon slag, which uses the gas-solid mixing device provided in the embodiment of the present invention to mix silicon slag and reaction gas, including the following steps:
[0083] First, the inert gas is used to pass through the mixing device at high speed to generate a negative pressure of about 2kpa at the inlet of the silicon slag and the reaction gas inlet, so that the silicon slag and the reaction gas are mixed evenly in the mixing device, wherein the flow rate of the inert gas The reaction gas is hydrogen chloride, and the material ratio of silicon slag to hydrogen chloride is 28:140.
[0084] Secondly, the mixed gas is reacted at a temperature of about 240°C, initially cooled at a temperature of about 130°C, and then secondary cooled at a temperature of 70°C to obtain chlorosilane gas. After the secondary cooling process, it will be deposited on The metal chlorides in the cooler are co...
Embodiment 2
[0087] This embodiment provides a method for producing chlorosilanes using organic silicon slag, which uses the gas-solid mixing device provided in the embodiment of the present invention to mix silicon slag and reaction gas, including the following steps:
[0088] First, the inert gas is used to pass through the mixing device at high speed to generate a negative pressure of about 20kpa at the inlet of the silicon slag and the reaction gas inlet, and then the silicon slag and the reaction gas are mixed evenly in the mixing device, wherein the flow rate of the inert gas is 300m / s, the reaction gas is hydrogen chloride, and the material ratio of silicon slag to hydrogen chloride is 56:140.
[0089] Secondly, the mixed gas is reacted at a temperature of about 350°C, initially cooled at a temperature of about 160°C, and then secondary cooled at a temperature of 130°C to obtain chlorosilane gas. After the secondary cooling process, it will be deposited on The metal chlorides in the...
Embodiment 3
[0092] This embodiment provides a method for producing chlorosilanes using organic silicon slag, which uses the gas-solid mixing device provided in the embodiment of the present invention to mix silicon slag and reaction gas, including the following steps:
[0093] First, the inert gas is used to pass through the mixing device at a high speed to generate a negative pressure of about 15kpa at the inlet of the silicon slag and the reaction gas inlet, so that the silicon slag and the reaction gas are mixed evenly in the mixing device, wherein the flow rate of the inert gas is 200m / s, the reaction gas is chlorine, and the material ratio of silicon slag to chlorine is 27:140.
[0094] Secondly, the mixed gas is reacted at a temperature of about 300°C, initially cooled at a temperature of about 150°C, and then secondary cooled at a temperature of 100°C to obtain chlorosilane gas. After the secondary cooling process, it will be deposited on The metal chlorides in the cooler are colle...
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Abstract
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