Bimetal composite oxide catalyst for change of methyl carbonate and phenol ester
A composite oxide, diphenyl carbonate technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, preparation of organic carbonates, etc., can solve environmental pollution, product separation and recovery difficulties, Difficulty in separation and recovery, etc., to achieve the effect of no environmental pollution, high catalytic activity and good stability
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Embodiment 1
[0030] Take 2g NH 4 VO 3 , add 20ml distilled water, then add 2ml 25% ammonia water, be mixed with solution; Get 2.044g basic copper carbonate in addition, make V / Cu (molar ratio)=1 / 1, add 20ml distilled water, be made into solution; The solutions were mixed and stirred, and the solution was evaporated to a sol state; the mixed product was dried in an oven at 110°C for 4 hours, and calcined in a muffle furnace at 550°C for 8 hours to obtain a bimetallic composite oxide catalyst. In a three-necked beaker connected with a nitrogen inlet tube, a constant pressure dropping funnel, a thermometer and a rectification column, add 0.45 g of the prepared catalyst and 15 g of phenol. When the temperature rises to 175°C, start to add dimethyl carbonate dropwise. The total amount of dimethyl carbonate added is 13.5ml. Calculate the reaction time from the start of adding dimethyl carbonate dropwise, and react for 9 hours; Azeotrope of Methanol and Dimethyl Carbonate. The mixed fraction a...
Embodiment 2
[0032] The preparation method of the catalyst is the same as in Example 1, and the molar ratio of vanadium and copper is adjusted to make V / Cu=1 / 0.5. The analysis method of reaction condition and product is the same as embodiment 1, and the activity result of catalyst is as follows: the conversion ratio of phenol is 28.39%, and the productive rate of methylphenyl carbonate and diphenyl carbonate is respectively 15.99% and 11.3%.
Embodiment 3
[0034]The preparation method of the catalyst is the same as in Example 1, and the molar ratio of vanadium and copper is adjusted to make V / Cu=1 / 0.25. The analysis method of reaction condition and product is the same as embodiment 1, and the activity result of catalyst is as follows: the conversion rate of phenol is 34.52%, and the productive rate of methylphenyl carbonate and diphenyl carbonate is respectively 16.81% and 16.64%.
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