Catalyst of synthetic propylene and application thereof
A technology of propylene carbonate and catalyst, applied in the field of catalyst for synthesizing propylene carbonate and its preparation, can solve the problems of high price, high toxicity and toxicity of crown ether, and achieves a catalyst with low cost, no environmental pollution, and not easy to be lost. Effect
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Embodiment 1
[0021] According to the composition (percentage by weight) of 20% potassium carbonate and 80% zirconia, the zirconia carrier is impregnated in the potassium carbonate solution, allowed to stand for 24 hours, dried at 120°C, and calcined at 600°C for 4 hours to obtain the catalyst. The cycloaddition reaction is carried out in an autoclave. Earlier in autoclave, add catalyzer, propylene oxide and methyl iodide, its add-on is potassium carbonate: propylene oxide: methyl iodide=0.01: 1: 0.025 (molar ratio), feeds the carbonic acid gas of 3.0MPa then, while stirring Under conditions, the temperature was raised to 150°C, and the reaction was carried out for 1 hour. After cooling, the residual gas was released and filtered to separate the catalyst from the reaction product. The reaction product was analyzed by gas chromatography. The conversion rate of propylene oxide was 99.4%, and the yield of propylene carbonate was 99.4%. was 98.1%.
Embodiment 2
[0023] 10% by potassium carbonate, alumina is 90% of the composition (percentage by weight) impregnated the alumina support in the potassium carbonate solution, let it stand for 24 hours, dried at 120°C, and roasted at 600°C for 4 hours to obtain the catalyst, and the remaining conditions With embodiment 1. The reaction conditions are as follows: pressure=3.0MPa, temperature=140 DEG C, potassium carbonate: propylene oxide: methyl iodide mol ratio=0.003: 1: 0.02, the reaction times is 1 hour, and reaction product is analyzed by gas chromatography, the conversion of propylene oxide The yield was 83.6%, and the yield of propylene carbonate was 80.1%.
Embodiment 3
[0025] Be 10% by potassium hydroxide, magnesia is 90% composition (percentage by weight) the magnesia carrier is impregnated in the potassium hydroxide solution, let stand for 24 hours, through 120 ℃ of drying, 600 ℃ of roasting 4 hours make catalyst, All the other conditions are with embodiment 1. Reaction condition is as follows: pressure=2.0MPa, temperature=120 ℃, potassium hydroxide: propylene oxide: methyl iodide mol ratio=0.003: 1: 0.02, the reaction times is 0.5 hour, and reaction product is through gas chromatography analysis, and the propylene oxide The conversion rate was 76.4%, and the yield of propylene carbonate was 72.3%.
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