Method for synthesizing cyclic carbonate by using carbon dioxide and epoxide
A cyclic carbonate and epoxide technology, applied in chemical instruments and methods, organic compounds/hydrides/coordination complex catalysts, chemical/physical processes, etc., can solve the problems of large usage of quaternary ammonium salts, etc. To achieve the effect of simple process, simple catalyst system and high activity
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Embodiment 1
[0021] Propylene oxide (29g), zinc molybdate catalyst (0.130g), and tetrabutylammonium bromide cocatalyst (0.241g) were added into an autoclave equipped with mechanical stirring and temperature-controlled heating device. Seal the reactor with CO 2 Replace the air in the kettle 3 times, then fill the reactor with CO 2 The initial pressure was 2.0MPa, the temperature was raised to 120°C, and the reaction was carried out for 1 hour. The reactor was cooled to room temperature, and the product propylene carbonate was separated by distillation under reduced pressure. Qualitative analysis was performed by GC-MS (HP 6890 / 5973), and quantitative analysis was completed by GC (Shanghai Analytical Instrument Company, GC-112A). See Table 1 for the conversion rate of raw material propylene oxide and the selectivity of product propylene carbonate.
Embodiment 2
[0023] Propylene oxide (29g), zinc molybdate catalyst (0.130g), and tetrabutylammonium bromide cocatalyst (0.161g) were added into an autoclave equipped with mechanical stirring and temperature-controlled heating device. Seal the reactor with CO 2 Replace the air in the kettle 3 times, then fill the reactor with CO 2 The initial pressure was 2.0MPa, the temperature was raised to 120°C, and the reaction was carried out for 1.5h. The reactor was cooled to room temperature, and the product propylene carbonate was separated by distillation under reduced pressure. Qualitative analysis was performed by GC-MS (HP 6890 / 5973), and quantitative analysis was completed by GC (Shanghai Analytical Instrument Company, GC-112A). See Table 1 for the conversion rate of raw material propylene oxide and the selectivity of product propylene carbonate.
Embodiment 3
[0025] Propylene oxide (29g), zinc molybdate catalyst (0.130g), and tetrabutylammonium bromide cocatalyst (0.323g) were added into an autoclave equipped with mechanical stirring and temperature-controlled heating device. Seal the reactor with CO 2 Replace the air in the kettle 3 times, then fill the reactor with CO 2 The initial pressure was 2.0MPa, the temperature was raised to 120°C, and the reaction was carried out for 0.5h. The reactor was cooled to room temperature, and the product propylene carbonate was separated by distillation under reduced pressure. Qualitative analysis was performed by GC-MS (HP 6890 / 5973), and quantitative analysis was completed by GC (Shanghai Analytical Instrument Company, GC-112A). See Table 1 for the conversion rate of raw material propylene oxide and the selectivity of product propylene carbonate.
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