A method for electrocatalytically synthesizing high-purity disilane
A technology of disilane and electrocatalysis, applied in the directions of silicon hydride, electrolysis components, electrolysis process, etc., can solve the problems of high price of hexachlorodisilane, high requirements on reaction devices, low yield of disilane, etc., and save reaction time. , the effect of saving the reaction process and improving the synthesis efficiency
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Embodiment 1
[0035] A method for synthesizing high-purity disilane, the process comprising:
[0036] (1) Feed monosilane as a raw material into an electrocatalytic reactor, and catalyze monosilane into disilane and hydrogen through electrocatalysis. The power supply voltage of the electrocatalytic reactor is controlled at 100-380V, the gas residence time is controlled at 10-60S, and the pressure is controlled at 0.3-1.2Mpa. After the one-way reaction of monosilane, the mixed gas of disilane, high silane, hydrogen and monosilane The gas enters the buffer tank and mixes evenly;
[0037] (2) The mixed gas in the buffer tank enters the compression device, and the compression device compresses the mixed gas to 0.5-2Mpa to meet the working pressure requirements of the gas-liquid separator, and the mixed gas becomes a gas-liquid mixture;
[0038] (3) Since the critical pressure of hydrogen is 1664.8kpa, the boiling point is -252.77℃, the critical pressure of disilane is 5150kpa, the boiling poin...
Embodiment 2
[0043] The synthesis system used in the above-mentioned processing method includes: an electrocatalytic reactor 1, a buffer tank 2, a gas compression device 3, a hydrogen separation device 4 and a disilane separation and purification device 5; wherein, the outlet of the electrocatalytic reactor 1 and the buffer tank 2 The inlet is communicated; the two ends of the gas compression device 3 are respectively communicated with the outlet of the buffer tank 2 and the inlet of the hydrogen separator 4; the top outlet of the hydrogen separator 4 is communicated with the inlet of the buffer tank 2, and the bottom outlet of the hydrogen separator 4 is connected with the The inlet of the disilane separation and purification device 5 is connected, and the top outlet of the disilane separation and purification device 5 is connected with the inlet of the electrocatalytic reactor 1 .
[0044] Wherein, electrocatalytic reactor 1 comprises: temperature detection device 11, pressure detection d...
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