System for producing silane, monochlorosilane, dichlorosilane and hexachlorodisilane
A technology of hexachlorodisilane and monochlorosilane, applied in the field of chemical synthesis, can solve the problems of limited development, no dichlorosilane and hexachlorodisilane, low selectivity and the like
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Embodiment 1
[0039] A system for producing silane, monochlorosilane, dichlorosilane and hexachlorodisilane, comprising: raw material synthesis system, silane synthesis system, monochlorosilane synthesis system, dichlorosilane synthesis system and hexachlorodisilane synthesis system; wherein , raw material synthesis system comprises hydrogenation system 1, disproportionation tower one 2, disproportionation tower two 3, condenser one 4 and condenser two 5; Wherein, condenser one 4 is fixed on the top of disproportionation tower one 2, and disproportionation tower one 2 Connected; condenser two 5 is fixed on the top of disproportionation tower two 3, and is communicated with disproportionation tower two 3; The inlet of hydrogenation system 1 is communicated with hexachlorodisilane synthesis system; Top outlet is communicated with the inlet of disproportionation tower one 2; Disproportionation tower The top outlet of disproportionation tower 2 is connected with the inlet of disproportionation t...
Embodiment 2
[0050] A method for producing silane, monochlorosilane, dichlorosilane and hexachlorodisilane, utilizes the system of embodiment 1 to produce, and the process is as follows:
[0051] 1) Send the raw materials hydrogen, silicon powder, and silicon tetrachloride into the hydrogenation system, and catalyze the synthesis of trichlorosilane through a catalyst; the reaction temperature is controlled at 100-800°C, the reaction pressure is controlled at 0.1-2MPa, and the catalyst is a transition metal salt , may be one of nickel, iron, copper, cobalt and zinc;
[0052] 2) Silicon trichloride enters the disproportionation tower 1 for disproportionation reaction, and is catalyzed by the disproportionation tower 1 catalyst to generate TCS and DCS. The mixed gas generated is rectified by the disproportionation tower 1. The silane enters the vaporizer from the tower kettle for separation; the light fraction enters the buffer tank from the upper part of the disproportionation tower one to o...
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