Method for purifying silicon tetrachloride by double-effect distillation
A silicon tetrachloride, double-effect rectification technology, applied in the field of rectification, can solve the problems of unfavorable production cost, high energy consumption, limited application, etc., and achieve the effects of secondary utilization, convenient process operation, and consumption saving
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Embodiment 1
[0029](1) The crude silicon tetrachloride obtained in the previous process first enters the spray tower, which is a two-stage spray, and the top condenser of the spray tower is a dephlegmator, and the gas phase produced by the dephlegmator is non-condensable gas And part of the crude silicon tetrachloride in the liquid phase condensed by the decondenser is refluxed, and part of it enters the light removal tower as the discharge material; out as solid impurities; the pressure at the top of the spray tower is normal pressure; (2) the gas phase extraction from the top of the light removal tower enters the reboiler of the weight removal tower as a heat source, and becomes liquid phase after heat exchange Part of the heat source is refluxed as the top reflux liquid of the light removal tower, and part of it is extracted as light component impurities; part of the crude silicon tetrachloride in the bottom of the light removal tower enters the reboiler of the bottom of the light remova...
Embodiment 2
[0036] (1) The crude silicon tetrachloride obtained in the previous process first enters the spray tower, which is a two-stage spray, and the top condenser of the spray tower is a dephlegmator, and the gas phase produced by the dephlegmator is non-condensable gas And part of the crude silicon tetrachloride in the liquid phase condensed by the decondenser is refluxed, and part of it enters the light removal tower as the discharge material; out as solid impurities; the pressure at the top of the spray tower is normal pressure; (2) the gas phase extraction from the top of the light removal tower enters the reboiler of the weight removal tower as a heat source, and becomes liquid phase after heat exchange Part of the heat source is refluxed as the top reflux liquid of the light removal tower, and part of it is extracted as light component impurities; part of the crude silicon tetrachloride in the bottom of the light removal tower enters the reboiler of the bottom of the light remov...
Embodiment 3
[0043] (1) The crude silicon tetrachloride obtained in the previous process first enters the spray tower, which is a two-stage spray, and the top condenser of the spray tower is a dephlegmator, and the gas phase produced by the dephlegmator is non-condensable gas And part of the crude silicon tetrachloride in the liquid phase condensed by the decondenser is refluxed, and part of it enters the light removal tower as the discharge material; out as solid impurities; the pressure at the top of the spray tower is normal pressure; (2) the gas phase extraction from the top of the light removal tower enters the reboiler of the weight removal tower as a heat source, and becomes liquid phase after heat exchange Part of the heat source is refluxed as the top reflux liquid of the light removal tower, and part of it is extracted as light component impurities; part of the crude silicon tetrachloride in the bottom of the light removal tower enters the reboiler of the bottom of the light remov...
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