Selective hydrogenation catalyst of aromatic aldehydes for refinement of terephthalic acid
A technology of terephthalic acid and hydrogenation catalysts, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, organic chemistry, etc., can solve the problem of low water solubility and hydrogen consumption of P-TA Large size, high separation energy consumption and other problems, to achieve the effect of reducing operating costs and energy consumption, reducing investment costs, and simplifying the process
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Embodiment 1
[0032] Weigh 50 grams of 4-8 mesh, flake-shaped coconut shell activated carbon, with a specific surface of 1078m 2 / g, the pore volume is 0.47ml / g. After removing the dust adsorbed on the carbon surface and the loose parts on the surface, pickle with 0.5N nitric acid in a washing tank at a washing temperature of 100°C for 1 hour, and then wash with deionized water until neutral. and dried at 120° C. for 2 hours before use. Take by weighing 0.5 gram of palladium-containing 20% chloropalladic acid solution, then add 4.05 gram of NiCl 2 .6H 2 O, then add an appropriate amount of surfactant and sodium carbonate, and finally add deionized water to dilute to the amount of the solution just submerged gac carrier is advisable. The catalyst active component solution is impregnated with the carrier, aged for 24 hours, then reduced with hydrogen, then washed with pure water until neutral and dried to obtain a catalyst product.
Embodiment 2
[0034] Catalyst preparation process and evaluation conditions are the same as in Example 1, wherein 0.75 gram of palladium-containing 20% chloropalladium acid solution is weighed, and the nickel added is 4.94 gram of Ni(NO 3 ) 2 .6H 2 O.
Embodiment 3
[0036] Catalyst preparation process and evaluation condition are the same as embodiment 1, and the nickel that adds is 1.06 gram Ni (CH 3 COO) 2 4H 2 O.
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