Catalyst to produce methyl methacrylate efficiently at low cost and preparation method of catalyst
A technology of methyl methacrylate and catalyst, which is applied in the direction of catalyst activation/preparation, carboxylate preparation, chemical instruments and methods, etc., which can solve the problem of unsatisfactory methacrolein MMA selectivity, high catalyst cost and affecting product quality and other problems, to achieve the effect of wide selection range, simple preparation process and low price
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Embodiment 1
[0032] Carrier molding conditions are the same as in Comparative Example 1.
[0033] Under stirring conditions, 250g chloroauric acid and 275g sodium citrate are fully mixed with 60L deionized water to obtain a stable, uniform and single gold sol with a higher dispersion state, and 280g polyvinylpyrrolidone (PVP, PVP, Molecular weight 8000-10000), then add 935g lanthanum nitrate, add 30kg above-mentioned prepared SiO after dissolving completely 2 -Al 2 o 3 -MgO powder, continue to stir and slowly raise the temperature to 75°C, continue to stir at this temperature for 14h and then cool down to room temperature, pour out the upper layer liquid after standing, wash the lower layer of precipitate with deionized water until no chloride ions are detected in the solution, 100°C After drying for 24 hours, it was calcined in air at 300°C for 24 hours to obtain the catalyst La-Au / SiO 2 -Al 2 o 3 -MgO. The mass percentages of La and Au in the catalyst are 1% and 0.48% respectively....
Embodiment 2
[0035] The carrier molding conditions are the same as in Comparative Example 1, wherein magnesium nitrate is replaced by rubidium nitrate, and spherical SiO with a particle size of about 70 μm is obtained. 2 -Al 2 o 3 - RbO powder, and then roast the powder at 700° C. in an air atmosphere for 6 hours, and cool it down to room temperature for use.
[0036] Catalyst preparation condition is the same as embodiment 1, obtains catalyst La-Au / SiO 2 -Al 2 o 3 -RbO, wherein the mass percentages of La and Au in the catalyst are 1% and 0.48% respectively.
Embodiment 3
[0038] The carrier molding conditions are the same as in Comparative Example 1, wherein magnesium nitrate is replaced with cesium nitrate to obtain spherical SiO with a particle size of about 70 μm 2 -Al 2 o 3 -CsO powder, and then calcined the powder at 700° C. in an air atmosphere for 6 hours, and cooled it down to room temperature for use.
[0039] Catalyst preparation condition is the same as embodiment 1, obtains catalyst La-Au / SiO 2 -Al 2 o 3 -CsO, wherein the mass percentages of La and Au in the catalyst are 1% and 0.48% respectively.
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