Clean production method of 2,4-di-tert-butylphenol
A di-tert-butylphenol, clean production technology, applied in the production of bulk chemicals, chemical instruments and methods, preparation of organic compounds, etc., can solve the problems of multi-industrial waste residue, poor selectivity, and inability to reuse
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Embodiment 1
[0041] 150 grams of phenol, 3 grams of molecular sieve catalyst (La 2 o 3 , CeO 2 The mass fractions are 5%, 5% respectively) into a 500ml four-necked flask, and the temperature is raised to 90°C for nitrogen displacement, and the isobutylene gas is started to flow to the bottom of the bottle. During the reaction, the temperature is maintained at 90-100°C, and the liquid After 4 hours of reaction, the flow of olefin was stopped, and the isobutylene tank was weighed, and the amount of olefin was calculated to be 195 grams. Analysis by gas chromatography showed that the conversion rate of phenol was 99.82%, 2, 4-di-tert-butylphenol selectivity 79.23%;
[0042] After the catalyst was recovered, 0.03 g of new catalyst was added and reacted again under the same conditions. The results showed that the conversion rate of phenol was 99.80%, and the selectivity of 2,4-di-tert-butylphenol was 78.93%;
[0043] The reaction result of the third use: the conversion rate of phenol is 99.8...
Embodiment 2
[0049] 150 grams of phenol, 3 grams of molecular sieve catalyst (La 2 o 3 , CeO 2 The mass fractions are 5%, 7% respectively) into a 500ml four-necked flask, and the temperature is raised to 100°C for nitrogen replacement, and the isobutylene gas is started to flow to the bottom of the bottle. During the reaction, the temperature is maintained at 100-120°C, and the liquid After 4 hours of reaction, the flow of olefin was stopped, and the isobutylene tank was weighed, and the amount of olefin was calculated to be 200 grams. Analysis by gas chromatography showed that the conversion rate of phenol was 99.90%, 2, 4-di-tert-butylphenol selectivity 77.63%;
[0050] After the catalyst was recovered, 0.05 g of new catalyst was added and reacted again under the same conditions. The results showed that the conversion rate of phenol was 99.85%, and the selectivity of 2,4-di-tert-butylphenol was 78.86%;
[0051] The reaction result of the third use: the conversion rate of phenol is 99....
Embodiment 3
[0054] 150 grams of phenol, 3 grams of molecular sieve catalyst (La 2 o 3 , CeO 2 The mass fractions are 7%, 7% respectively) into a 500ml four-necked flask, and the temperature is raised to 120°C for nitrogen replacement, and the isobutylene gas is started to flow to the bottom of the bottle. During the reaction, the temperature is kept at 120-130°C, and the liquid After 4 hours of reaction, the flow of olefin was stopped, and the isobutylene tank was weighed, and the amount of olefin was calculated to be 195 grams. Analysis by gas chromatography showed that the conversion rate of phenol was 99.22%, 2, 4-di-tert-butylphenol selectivity 77.29%;
[0055] After the catalyst was recovered, 0.04 g of new catalyst was added and reacted again under the same conditions. The results showed that the conversion rate of phenol was 99.83%, and the selectivity of 2,4-di-tert-butylphenol was 78.93%;
[0056] The reaction result of the third use: the conversion rate of phenol is 99.83%, a...
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