Method and device for producing high-purity boron tribromide
A technology of boron tribromide and a production method, which is applied to boron halide compounds, boron halides and other directions, can solve the problems of poor product quality and color, can not meet high-purity requirements, etc., and achieves the effect of smooth production process and reduced production cost.
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Embodiment 1
[0044] Put 12kg of industrial boron carbide with a purity of 97% and a particle size of 1 to 3 mm into multiple quartz reactors in reactor 3, with a total reaction cross-sectional area of 130 cm 2 , the temperature of the reaction furnace is raised to 650°C; 120kg of liquid bromine is put into the vaporization kettle 1 for heating and vaporization, the vaporization temperature is 120°C, and the vaporized red bromine vapor has a pressure of 0.1MPa and a flow rate of 0.4m 3 Nitrogen per hour is introduced into the drier 2 and dehydrated and dried by anhydrous calcium chloride with a particle size of 1mm and a purity of 96%, and then enters the quartz reaction furnace from the bottom of the reaction furnace 3 for bromination reaction; the tribromine produced by the reaction The boron gas comes out from the top of the reaction furnace and enters the soot trap 4; boron tribromide enters from the middle of the primary glass column 42 through the inlet 41, and the gas phase and liqu...
Embodiment 2
[0048] Put 12kg of industrial boron carbide with a purity of 97% and a particle size of 1 to 3 mm into the quartz reaction furnace of the reaction furnace 3, with a total reaction cross-sectional area of 130 cm 2 , the temperature of the reaction furnace is raised to 850°C; 120kg of liquid bromine is put into the vaporization kettle 1 to be heated and vaporized, the vaporization temperature is 120°C, and the vaporized red bromine vapor has a pressure of 0.3MPa and a flow rate of 0.8m 3 Nitrogen per hour is introduced into the drier 2 and dehydrated and dried by anhydrous calcium chloride with a particle size of 1mm and a purity of 96%, and then enters the quartz reaction furnace from the bottom of the reaction furnace 3 for bromination reaction; the tribromine produced by the reaction The boron gas comes out from the top of the reaction furnace and enters the soot trap 4; boron tribromide enters from the middle of the primary glass column 42 through the inlet 41, and the gas ...
Embodiment 3
[0052] Put 12kg of industrial boron carbide with a purity of 97% and a particle size of 1 to 3 mm into the quartz reaction furnace of the reaction furnace 3, with a total reaction cross-sectional area of 130 cm 2 , the temperature of the reaction furnace is raised to 720°C; 120kg of liquid bromine is put into the vaporization kettle 1 to be heated and vaporized, the vaporization temperature is 120°C, and the vaporized red bromine vapor has a pressure of 0.2MPa and a flow rate of 0.6m 3Nitrogen per hour is introduced into the drier 2 and dehydrated and dried by anhydrous calcium chloride with a particle size of 1mm and a purity of 96%, and then enters the quartz reaction furnace from the bottom of the reaction furnace 3 for bromination reaction; the tribromine produced by the reaction The boron gas comes out from the top of the reaction furnace and enters the soot trap 4; boron tribromide enters from the middle of the primary glass column 42 through the inlet 41, and the gas p...
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