Method for coproduction of methyl isobutyl ketone and methyl isobutyl carbinol
A technology of methyl isobutyl ketone and methyl isobutyl ketone, applied in the field of producing methyl isobutyl ketone, can solve the problems of low selectivity and low yield of methyl isobutyl methanol, and achieve high product yield , the effect of high utilization and simple equipment
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Embodiment 1
[0035] The reactor is equipped with the brand BC-A-61 catalyst produced by Beijing Research Institute of Chemical Industry.
[0036] The reaction temperature is 180° C., the reaction pressure is 2.3 MPa, the liquid space velocity of acetone is 1.0 L acetone / (L catalyst·hour), and the molar ratio of acetone:hydrogen is 1:0.4. Reaction result: the conversion rate of acetone is 55%, the selectivity of methyl isobutyl ketone is 80%, the selectivity of methyl isobutyl carbinol is about 19.0%
Embodiment 2
[0038] Use catalyst in the reactor with embodiment 1.
[0039] The reaction temperature is 195° C., the reaction pressure is 2.5 MPa, the liquid space velocity of acetone is 1.3 L acetone / (L catalyst·hour), and the molar ratio of acetone:hydrogen is 1:0.5. Reaction result: the conversion rate of acetone is 60%, the selectivity of methyl isobutyl ketone is 74%, and the selectivity of methyl isobutyl carbinol is about 24.0%.
Embodiment 3
[0041] Use catalyst in the reactor with embodiment 1.
[0042] The reaction temperature is 205° C., the reaction pressure is 2.8 MPa, the liquid space velocity of acetone is 1.6 L acetone / (L catalyst·hour), and the molar ratio of acetone:hydrogen is 1:0.6. Reaction result: the conversion rate of acetone is 66%, the selectivity of methyl isobutyl ketone is 70%, and the selectivity of methyl isobutyl carbinol is about 28.0%.
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