Preparation method of catalyst for improving the yield of n-butane oxidation to maleic anhydride
A catalyst and n-butane technology, applied in physical/chemical process catalysts, chemical instruments and methods, organic chemistry, etc., can solve problems affecting catalyst performance and low specific surface area of catalysts, and achieve the effect of improving contact and increasing activity
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Embodiment 1
[0024] Add 1 part of vanadium pentoxide, 1 part of phosphoric acid (100%wt), 0.05 part of zinc acetylacetonate and 300ml of isobutanol solution into a four-neck flask, heat to reflux, and react for 3 hours at a stirring speed of 300r / min. Add 0.3 parts of P123 into the reaction system, continue to stir and reflux for 10 hours, stop heating and filter the mixed solution, heat-treat the filter cake at 400°C to obtain a catalyst with a specific surface area of 28m 2 / g. Gained catalyst is reacted with the butane raw material whose molar concentration is 1.5% mol, and its reaction process condition: 2000hr -1 Space velocity and 400°C normal pressure were evaluated in a fixed-bed reactor, and the conversion rate of butane was measured to be 84.5%, and the yield of maleic anhydride was 60.2%. The evaluation results are shown in Table 1.
Embodiment 2
[0026] Add 1 part of vanadium pentoxide, 1 part of phosphoric acid (100%wt), 0.05 part of zinc acetylacetonate and 300ml of isobutanol solution into a four-neck flask, heat to reflux, and react for 3 hours at a stirring speed of 300r / min. Add 0.3 parts of Brij-56 into the reaction system, continue to stir and reflux for 10 hours, stop heating and filter the mixed solution, heat-treat the filter cake at 400°C to obtain a catalyst with a specific surface area of 29m 2 / g. Gained catalyst is reacted with the butane raw material whose molar concentration is 1.5% mol, and its reaction process condition: 2000hr -1 Space velocity and 400°C normal pressure were evaluated in a fixed-bed reactor, and the conversion rate of butane was measured to be 84.7%, and the yield of maleic anhydride was 60.4%. The evaluation results are shown in Table 1.
Embodiment 3
[0028] Add 1 part of vanadium pentoxide, 1 part of phosphoric acid (100%wt), 0.05 part of zinc acetylacetonate and 300ml of isobutanol solution into a four-neck flask, heat to reflux, and react for 3 hours at a stirring speed of 300r / min. Add 0.3 parts of pentaerythritol ester into the reaction system, continue to stir and reflux for 10 hours, stop heating and filter the mixed solution, then heat-treat the filter cake at 400°C to obtain a catalyst with a specific surface area of 29m 2 / g. Gained catalyst is reacted with the butane raw material whose molar concentration is 1.5% mol, and its reaction process condition: 2000hr -1 Space velocity and 400°C normal pressure were evaluated in a fixed-bed reactor, and the conversion rate of butane was measured to be 84.2%, and the yield of maleic anhydride was 60.5%. The evaluation results are shown in Table 1.
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