Clapboard adsorption device and method for removing boron impurities in chlorosilane system
An adsorption device, chlorosilane technology, applied in halosilanes, halogenated silicon compounds, fractionation and other directions, to achieve the effect of reducing energy consumption, simplifying process flow, reducing energy consumption and equipment costs
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example 1
[0022] The chlorosilane system contains 95.0% trichlorosilane, 2.0% silicon tetrachloride, 2.0% dichlorodihydrosilane and 1.0% boron trichloride. The throughput of raw material is 378.8kg / hr, which translates to a molar flow rate of 2.8Kmol / hr. The tower adsorption section adopts ion exchange resin adsorbent with high adsorption capacity. The main tower adopts metal mesh corrugated packing.
[0023] The pressure at the top of the tower is 300Kpa, the temperature at the top of the tower is 49.2°C, the thermal condition of the feed is 30.0°C, and the bubble point feed is fed. The heat load is 0.0120M*kcal / hr, the reboiler heat load is 0.0154M*kcal / hr, the number of theoretical plates in the public rectification section is 19, the number of theoretical plates in the public stripping section is 9, the number of theoretical plates in the tower adsorption section is 10, and the side line The number of theoretical plates in the production section is 20, and the reflux ratio is 35. ...
example 2
[0026] Contain 98% trichlorosilane in the chlorosilane system, 0.8% silicon tetrachloride, 0.7% dichlorodihydrosilane, 0.5% boron trichloride, the processing capacity of raw material is 379.1kg / hr, is converted into The molar flow rate is 2.8 Kmol / hr. The tower adsorption section adopts zeolite molecular sieve adsorbent.
[0027] The pressure at the top of the tower is 400Kpa, the temperature at the top of the tower is 70.8°C, and the thermal condition of the feed is 30.0°C. The heat load of the reboiler is 0.0153M*kcal / hr, and the heat load of the reboiler is 0.0199M*kcal / hr. The number of theoretical plates in the section is 20, and the reflux ratio is 45.
[0028] The yield of trichlorosilane is 72.1%, the purity of trichlorosilane is 99.1%, the content of B is 0.11%, and the removal efficiency of B is 84.0%. And use two towers to remove light and heavy to simulate when reaching trichlorosilane purity 99.1% and when the removal efficiency of B is 84.0%, trichlorosilane y...
example 3
[0030] The chlorosilane system contains 95.0% trichlorosilane, 2.0% silicon tetrachloride, 2.0% dichlorodihydrosilane and 1.0% boron trichloride. The throughput of raw material is 378.8kg / hr, which translates to a molar flow rate of 2.8Kmol / hr. The tower adsorption section uses silica gel as the adsorbent.
[0031] The pressure at the top of the tower is 500Kpa, the temperature at the top of the tower is 65.3°C, and the thermal condition of the feed is 30.0°C. The heat load of the reboiler is 0.0143M*kcal / hr, and the heat load of the reboiler is 0.0197M*kcal / hr. The number of theoretical plates in the section is 20, and the reflux ratio is 45.
[0032] The yield of trichlorosilane is 73.0%, the purity of trichlorosilane is 97.6%, the B content is 0.25%, and the removal efficiency of B is 82.0%. And when using two towers to remove light and heavy to simulate, when reaching the removal efficiency of trichlorosilane purity 97.6% and B is 82.0%, the yield of trichlorosilane is ...
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