Catulyst for preparing propionic acid by propionaldehyde oxidation and its method
An oxidation system and catalyst technology, applied in the direction of physical/chemical process catalysts, chemical instruments and methods, organic compounds/hydrides/coordination complex catalysts, etc., can solve the problem of raw material consumption quotas and high production costs, propionic acid selectivity And low yield, poor product quality and other problems, to achieve the effect of improving yield and quality, improving catalytic activity, and reducing pressure
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Embodiment 1
[0027] Example 1. Put 1000 parts by weight of propionaldehyde in a reactor, add 1 part by weight of cobalt propionate and 2 parts by weight of phosphoric acid, and mix them thoroughly in the reactor. Feed nitrogen into the reactor to make the pressure 0.4MPa, heat, stir, feed oxygen to make the pressure 0.6~2.0MPa, and react at 90~100°C for 2 hours. Cool to room temperature, and rectify the product in the kettle under normal pressure to collect the distillate at 138~142°C as propionic acid. The conversion rate of propionaldehyde was 96%, the selectivity of propionic acid was 98%, and the yield of propionic acid was 95%.
Embodiment 2
[0028] Example 2: Put 1000 parts by weight of propionaldehyde in the reactor, add 1 part by weight of manganese propionate and 3 parts by weight of phosphoric acid, and fully mix them in the reactor. Feed nitrogen into the reactor to make the pressure 0.4MPa, heat, stir, feed oxygen to make the pressure 0.6~1.8MPa, and react at 80~100°C for 2.5 hours. Cool to room temperature, and rectify the product in the kettle under normal pressure to collect the distillate at 138~142°C as propionic acid. The conversion rate of propionaldehyde was 96%, the selectivity of propionic acid was 97%, and the yield of propionic acid was 94%.
Embodiment 3
[0029] Example 3: Put 1000 parts by weight of propionaldehyde in the reactor, add 1 part by weight of cobalt naphthenate and 6 parts by weight of phosphoric acid, and mix them thoroughly in the reactor. Feed nitrogen into the reactor to make the pressure 0.4 MPa, heat, stir, feed air to make the pressure 0.6~2.0 MPa, and react at 80~100°C for 3 hours. Cool to room temperature, and rectify the product in the kettle under normal pressure to collect the distillate at 138~142°C as propionic acid. The conversion rate of propionaldehyde was 95%, the selectivity of propionic acid was 97%, and the yield of propionic acid was 92%.
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