Disilane manufacturing method
A manufacturing method and technology of disilane, applied in chemical instruments and methods, silicon hydride, molecular sieve catalysts, etc., can solve problems such as preparation, and achieve the effects of reducing production cost, improving production efficiency, and low energy consumption
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Embodiment 1
[0020] Disilane is produced according to the above method. Wherein, the reaction temperature is -10°C, the reaction pressure is 0.2 MPa, the molar ratio of the magnesium silicide and the ammonia chloride is 1:2, and the catalyst is C 54 H 52 P 4 ZnCl 2 , The reaction is in 3M 3 In the reactor. The purification device is two stainless steel vessels with a diameter of 10 cm and a height of 1 m connected in series. A copper-based catalyst is arranged in the purification device. The copper-based catalyst is a supported catalyst, and the carrier of the catalyst is a titanium silicate molecular sieve with a pore size of 0.2 nm.
Embodiment 2
[0022] Example 1 was repeated, except that the reaction temperature was 50° C., the reaction pressure was 1 MPa, the molar ratio of magnesium silicide to ammonia chloride was 1:5, and the catalyst was C 54 H 45 P 3 ZnX 2 , The reaction is at 10M 3 It is carried out in a reaction kettle equipped with a magnetic stirrer. The purification device is two stainless steel vessels with a diameter of 40 cm and a height of 3 m connected in series. A cuprous chloride catalyst is arranged in the purification device. The support for the cuprous chloride is a silica molecular sieve with a pore size of 50 nm.
Embodiment 3
[0024] Example 1 was repeated, except that the reaction temperature was 20° C., the reaction pressure was 0.6 MPa, the molar ratio of magnesium silicide to ammonia chloride was 1:3.5, and the catalyst was C 52 H 48 P 4 ZnCl 2 , The reaction is at 6.5M 3 It is carried out in a reaction kettle equipped with a magnetic stirrer. The purification device is 4 series-connected stainless steel vessels with a diameter of 20 cm and a height of 2 m. A catalyst of copper and cuprous chloride is arranged in the purification device. The molar ratio of copper and cuprous chloride is 3:1, and the catalyst support is a silica molecular sieve with a pore size of 1 nm.
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