Catalyst for preparing cyclohexane carboxylic acid through benzoic acid hydrogenation and preparation method and application thereof
A cyclohexanecarboxylic acid and catalyst technology, applied in metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, preparation of carboxylic acid by ozone oxidation, etc., can solve the problem of high unit consumption of precious metal palladium and decreased reaction selectivity , the increase of secondary reactions and other problems, to achieve the effect of less precious metal dosage, strong poisoning ability and simple preparation method
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Embodiment 1
[0022] Crush the nickel foam sheet into 20-60 mesh particles, rinse with organic solvent for 50 minutes to remove oil, rinse with water, soak in dilute hydrochloric acid for 40 minutes, wash with water and set aside. Mix 3 parts of 40% formaldehyde aqueous solution, 3 parts of phenol, 0.06 parts of sodium hydroxide and 93.94 parts of water, and react at 85°C for 10 minutes to obtain phenolic resin slurry. Take 7 parts of phenolic resin slurry, add 3 parts of ethanol and mix to make phenolic resin immersion solution.
[0023] Soak the nickel foam in the phenolic resin immersion solution for 10 minutes, dry it, and cure it at a temperature of 240°C for 30 minutes, and then carbonize it from a low temperature to a high temperature within 120 minutes under a temperature gradient of 240-900°C; after the carbonization is completed , at 600°C, activated by passing water vapor to obtain an additive-coated nickel foam carrier, in which activated carbon accounts for 9.8wt% of the weight...
Embodiment 2
[0026] Except that ethanol is not contained in the phenolic resin immersion solution, all the other steps are the same as in Example 1. In the obtained catalyst, the activated carbon accounted for 14.1 wt% of the nickel foam weight, and the Pd accounted for 1 wt% of the sum of the carrier and the additive.
Embodiment 3
[0028] Except that the resin slurry: ethanol in the phenolic resin immersion solution was changed to 1:1, the rest of the steps were the same as in Example 1. In the obtained catalyst, the activated carbon accounted for 4.5wt% of the nickel foam weight, and the Pd accounted for 1wt% of the sum of the carrier and the auxiliary agent.
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