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ChemicalBook CAS DataBase List Hexamethyldisilazane
999-97-3

Hexamethyldisilazane synthesis

11synthesis methods
A production method for hexamethyldisilazane comprises the following steps: trimethylsilyl chloride is added into a sealed reaction kettle with a bearing pressure higher than 0.5MPa, stirring is carried out, ammonia gas is introduced, the ammonia pressure in the reaction kettle is maintained at a value between 0.1MPa and 0.2MPa, the temperature is between 40 ℃ and 50 ℃, the reaction is carried out, and the ammonia gas quantity is gradually reduced till the stop; and then, the pressure is maintained at the unchanged value between 0.1MPa and 0.2MPa, the reaction is maintained for 0.5h to 2h, then, the temperature in the kettle is lowered to a value below 10 ℃, water with the temperature lower than 10 ℃ is added, the dissolution reaction is carried out to generate ammonia chloride, and upper layer materials are hexamethyldisilazane after the delamination.
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Yield:999-97-3 97.3%

Reaction Conditions:

with ammonia at 50; under 1425.14 Torr; for 2.5 h;Temperature;Pressure;

Steps:

9

1 L of chlorotrimethylsilane was added to the reactor equipped with a stirrer, thermometer and pressure gauge. Stir well. Recanalize ammonia gas into the reaction. The total amount of ammonia gas was 1.6 L, the reaction temperature was controlled at 30°C, the reaction pressure is 0.15 Mpa, control reaction time is 0.5h, the rate of introduction of ammonia was 0.5 L / min. As the reaction progresses, more solid byproduct ammonium chloride is formed. Material gradually becomes a paste. Open the reactor bottom valve. Discharge processing. With the mortar pump to hit the reaction material within the frame filter press. The ammonium chloride solids are retained in the filter press. The clear liquid flow back to the reactor to continue the reaction in the manner described above. Circularly processed twice. The third time back to the reaction tank of clarified liquid reaction. The reaction mixture was removed from the reaction kettle. The reaction mixture was filtered. Remove the residue to obtain a filtrate. Finally, the obtained filtrate is analyzed and detected. The remaining amount of chlorotrimethylsilane in the filtrate was examined. The residual amount of chlorotrimethylsilane is brought to a predetermined value. The total time to complete the reaction was 2 h. After completion of the reaction, continue to fight the material filter. From the frame filter out of the clear liquid is no longer back to the reactor, but into the crude product receiving tank. Crude products after alkali washing to distillation, the product hexamethyldisilazane. The content of hexamethyldisilazane was 99.0% and the yield was 95.4% (molar yield).
In Examples 2-15, the reaction was carried out in the same manner as in Example 1 except changing trimethylchlorosilane, ammonia, the ammonia gas flow rate, reaction time, reaction temperature and reaction pressure. Specific formulations in Table 1. Specific process conditions, the amount of phase transfer catalyst and product yield are shown in Table 2.
Example 9; chlorotrimethylsilane 1.3 L; ammonia 2.14 L; ammonia gas flow rate 1.2 L / min
Example 9; Overall reaction time 2.5 h; Reaction temperature 50°C; Reaction pressure 0.19 MPa; Yield 97.3%

References:

CN105732688,2016,A Location in patent:Paragraph 0034; 0036; 0038; 0041

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