Method for preparing o-cresol
A technology for o-cresol and phenol, applied in the field of preparing o-cresol, can solve the problem of low selectivity of o-cresol, and achieve the effects of long service life, high selectivity and simple process
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Embodiment 1
[0025] Catalyst preparation: Weigh Fe(NO 3 ) 3 9H 2 O 404g, Mg(NO 3 ) 2 ·6H 2 O 51.2g and Ce(NO 3 ) 3 ·6H 2 O 2.17g was mixed and dissolved in 800mL ethanol, and then it was slowly mixed with 28% concentrated ammonia water 700mL containing 4g PEG in a co-current manner under normal temperature ultrasonic conditions, and the ultrasonic wave was continued for 30min after the addition, and then the precipitate was filtered. Wash and dry at 120°C for 6h. The obtained solid is then roasted at 450°C for 8 hours, and finally the solid is ground into fine particles, and then crushed into small particles of 10 to 20 meshes after tableting. The obtained basic metal oxide catalyst is Fe 1 Mg 0.2 Ce 0.05 / o.
[0026] The above-mentioned catalyst was packed in a Φ7mm stainless steel reaction tube, the catalyst loading amount was 5g, the reaction mixture was metered in with an advection pump, and the temperature was controlled by a temperature control device. Feed space velocity...
Embodiment 2
[0031] Catalyst is the same as embodiment 1, reaction mixture phenol: xylenol: methyl alcohol: water=34: 10: 38: 18 (wt%), carrier gas helium flow rate is 40mL / min, changes feeding space velocity, other conditions are implemented with Example 1, after 12 hours of reaction, sampling was carried out for chromatographic analysis. There were no impurities such as p-cresol and anisole, and the selectivity of o-cresol was more than 95.2%. The results are shown in Table 2.
[0032] Table 2 changes the result of feed space velocity synthesis o-cresol
[0033]
Embodiment 3
[0035] The catalyst is the same as in Example 1, and the catalyst is filled with 40mL and weighs 36.5g. The reaction tube is a Φ16×1200mm stainless steel tube. Reaction mixture phenol:xylenol:methanol:water=34:10:38:18 (wt%), space velocity 1.2h -1 , atmospheric pressure, carrier gas N 2 The flow rate was 120mL / min, and the reaction was carried out continuously for 500h (excluding regeneration). The results are shown in Table 3. The average conversion rate of phenol was 33.4%, and the selectivity of o-cresol was 96.0%.
[0036] Table 3 Catalyst Activity Stability Investigation Results
[0037]
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