Method for synthesizing methoxyacetone by 1-methoxy-2-propanol gas phase oxidation dehydrogenation
A gas-phase dehydrogenation technology of methoxyacetone, which is applied in the field of chemical industry, can solve the problems of low selectivity, difficulty in oxidation of 1-methoxy-2-propanol, difficulty in separation of methoxyacetone, etc. simple effect
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Embodiment 1
[0015] Adopt 3.0g electrolytic silver catalyst, 1-methoxy group-2-propanol and oxygen are raw materials, the volume fraction that nitrogen occupies after nitrogen dilution is 89.8%, raw material reacts in stainless steel fixed-bed reactor after vaporization, reaction temperature 300°C, Feed Oxygen Alcohol Ratio 1.25, Liquid Hourly Space Velocity 5.45h -1 , the conversion rate of 1-methoxy-2-propanol is 68.83%, and the selectivity of product methoxyacetone is 73.02%.
Embodiment 2
[0017] Adopt 3.0g electrolytic silver catalyst, 1-methoxy group-2-propanol and oxygen are raw materials, the volume fraction that nitrogen occupies after nitrogen dilution is 89.8%, raw material reacts in stainless steel fixed-bed reactor after vaporization, reaction temperature 465°C, Feed Oxygen Alcohol Ratio 1.25, Liquid Hourly Space Velocity 5.45h -1 , the conversion rate of 1-methoxy-2-propanol is 96.77%, and the selectivity of product methoxyacetone is 62.29%.
Embodiment 3
[0019] Adopt 3.0g electrolytic silver catalyst, 1-methoxy group-2-propanol and air are raw material, the volume fraction that nitrogen occupies after nitrogen dilution is 89.0%, raw material reacts in stainless steel fixed-bed reactor after vaporization, reaction temperature 600°C, Feed Oxygen Alcohol Ratio 1.25, Liquid Hourly Space Velocity 5.45h -1 , the conversion rate of 1-methoxy-2-propanol is 91.14%, and the selectivity of the product methoxyacetone is 33.40%.
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