Preparation method of shape-selective catalyst for synthesizing p-methyl phenol
A p-alkylphenol and catalyst technology, which is applied in the field of preparation of shape-selective catalysts in the process of synthesizing p-cresol, can solve the problems of reducing the para-position shape selectivity of the catalyst, increasing the selectivity of o-cresol, and achieving low cost , high shape-selective performance, and high catalytic activity
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Embodiment 1
[0016] Take metal lithium nitrate (3.25g), add (39.8ml) in dehydrated alcohol, wherein the mass ratio of metal nitrate and dehydrated alcohol is 1:10, treat that it dissolves completely and then add complex ligand Tetramethyl Ethylenediamine (16.43g), wherein the mol ratio of complex ligand and lithium ion in lithium nitrate is 3:1, stirs with glass rod, then (4.0g) microporous molecular sieve MCM-22 is added wherein, Make the mass ratio of lithium ions in lithium nitrate to microporous molecular sieves 1:13.3, stir evenly, soak at room temperature for 24 hours, dry in a water bath at 60°C, then transfer to an oven to dry at 120°C for 6 hours, and then put Calcined in a muffle furnace, the temperature was raised to 550 °C at 10 °C / min and kept for 6 h to obtain a shape-selective catalyst with a lithium ion loading of 7.5%. The catalyst was used in the process of alkylation of phenol and dimethyl carbonate to synthesize p-cresol, the molar ratio was phenol:dimethyl carbonate 1:...
Embodiment 2
[0018] Compared with Example 1, the molar ratio of lithium ions in the complex ligand tetramethylethylenediamine and lithium nitrate was changed to 1:1, and the others were the same. The catalyst was used in the process of alkylation of phenol and dimethyl carbonate to synthesize p-cresol, the molar ratio was phenol:dimethyl carbonate 1:1, the reaction temperature was 360 °C, and the mass space velocity of the raw material was 2 h -1 , the conversion rate of phenol reached 82.6%, and the selectivity to p-cresol was 70.1%.
Embodiment 3
[0020] Compared with Example 1, the mass ratio of lithium ions to microporous molecular sieves in lithium nitrate was changed to 1:100, that is, the lithium ion loading was 1%, and the others were the same. The catalyst was used in the process of alkylation of phenol and dimethyl carbonate to synthesize p-cresol, the molar ratio was phenol:dimethyl carbonate 1:1, the reaction temperature was 360 °C, and the mass space velocity of the raw material was 2 h -1 , the conversion rate of phenol reaches 90.7%, and the selectivity to p-cresol is 45.2%.
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