Purification method of low-pollution high-purity electronic grade polycrystalline silicon
A purification method and electronic-grade technology, which is applied in the direction of chemical instruments and methods, silicon hydride, silicon compounds, etc., can solve problems such as the impact on the purity of silane products, and achieve the effect of improving purity, reducing production costs and energy consumption
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Embodiment 1
[0028] (1) The prepared crude silane is introduced into the first rectification tower through a gas compressor. The temperature inside the first rectification tower is -32°C, operated at 2.2 MPa, and light is separated from the top of the first rectification tower. Components, light components include hydrogen, ammonia and methane, and the rest come from the bottom fraction of the first rectification tower.
[0029] (2) At -32°C, the rest of the bottom fraction of the first rectification tower is directly introduced into the 4A molecular sieve adsorption column, and the internal pressure of the 4A molecular sieve adsorption column is controlled to 1.17MPa. Ethylene is removed, and the remaining unremoved ethylene is converted into ethylsilane, and the part after the adsorption is completed is discharged from the top of the 4A molecular sieve adsorption column.
[0030] (3) Introduce the part discharged from the top of the 4A molecular sieve adsorption column into the second re...
Embodiment 2
[0034] (1) The crude silane produced is introduced into the first rectification tower through a gas compressor. The temperature inside the first rectification tower is -33°C, operated at 2.1 MPa, and light is separated from the top of the first rectification tower. Components, light components include hydrogen, ammonia and methane, and the rest come from the bottom fraction of the first rectification tower.
[0035] (2) At -27°C, the rest of the bottom fraction of the first rectification tower is directly introduced into the 4A molecular sieve adsorption column, and the internal pressure of the 4A molecular sieve adsorption column is controlled to 1.37MPa, and most of the 4A molecular sieve adsorption column is Ethylene is removed, and the remaining unremoved ethylene is converted into ethylsilane, and the part after the adsorption is completed is discharged from the top of the 4A molecular sieve adsorption column.
[0036](3) Introduce the part discharged from the top of the ...
Embodiment 3
[0040] (1) The crude silane produced is introduced into the first rectification tower through a gas compressor. The temperature inside the first rectification tower is -32°C, operated at 2.0 MPa, and light is separated from the top of the first rectification tower. Components, light components include hydrogen, ammonia and methane, and the rest come from the bottom fraction of the first rectification tower.
[0041] (2) At -37°C, the rest of the bottom fraction of the first rectification tower is directly introduced into the 4A molecular sieve adsorption column, and the internal pressure of the 4A molecular sieve adsorption column is controlled to 1.48MPa, and most of the 4A molecular sieve adsorption column is Ethylene is removed, and the remaining unremoved ethylene is converted into ethylsilane, and the part after the adsorption is completed is discharged from the top of the 4A molecular sieve adsorption column.
[0042] (3) Introduce the part discharged from the top of the...
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