Catalyst for selectively oxidizing tertiary butanol or isobutene to synthesize methyl acrylic aldehyde and its use
A technology for synthesizing methacrolein and methacrolein, which is used in physical/chemical process catalysts, preparation of organic compounds, preparation of carbon-based compounds, etc., can solve the problem of shortening the service life of catalysts, deterioration of catalyst performance, catalyst activity or selection Sexual decline, etc.
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Embodiment 1
[0018] One with 80 (Mo 12 Bi 1.8 Fe 2.0 co 7.0 Sb 0.3 Pb 0.2 Yb 0.1 W 0.5 sn 0.2 Cs 0.5 ) / 20TiO 2 The preparation method of the indicated catalyst (the atomic ratio of the metal elements constituting the active component and the carrier heat-conducting diluent) is as follows: 322.56 grams of ammonium paramolybdate and 21.58 grams of ammonium paratungstate are dissolved in 800 grams of distilled water at a temperature of 50 ° C to obtain a solution First. 122.22 grams of bismuth nitrate, 113.12 grams of ferric nitrate, 285.18 grams of cobalt nitrate, 9.38 grams of lead nitrate, 13.65 grams of cesium nitrate and 2.76 grams of ytterbium oxide were dissolved in 350 grams of 15% by weight dilute nitric acid aqueous solution to obtain solution B. 13.16 grams of antimony pentachloride and 6.30 grams of tin dichloride were dissolved in 30 grams of 10% by weight dilute hydrochloric acid aqueous solution to obtain solution C. Add solutions B and C to solution A respectively u...
Embodiment 2
[0021] In addition to using 8.19 grams of ammonium metavanadate and 8.33 grams of zinc nitrate to replace 21.58 grams of ammonium paratungstate and 6.30 grams of tin dichloride, 20 grams of nano-metal titanium powder was used to replace 20 grams of TiO 2 , and all the other are prepared catalysts by the same method as in Example 1. The catalyst consists of:
[0022] 80 (Mo 12 Bi 1.8 Fe 2.0 co 7.0 Sb 0.3 Pb0.2 Yb 0.1 V 0.5 Zn 0.2 Cs 0.5 ) / 20Ti
[0023] According to the same method as in Example 1, the catalyst was used for oxidation reaction at 398°C (hot spot). The conversion of isobutene was 96.2%, the selectivity of MAL was 86.7%, the selectivity of MAA was 2.1%, and the total yield of MAL and MAA was 85.4%.
Embodiment 3
[0025] In addition to replacing 21.58 grams of ammonium paratungstate with 9.31 grams of niobium pentoxide, 20 grams of SiC was used to replace 20 grams of TiO during molding. 2 , and all the other are prepared catalysts by the same method as in Example 1. The catalyst consists of:
[0026] 80 (Mo 12 Bi 1.8 Fe 2.0 co 7.0 Sb 0.3 Pb 0.2 Yb 0.1 Nb 0.5 sn 0.2 Cs 0.5 ) / 20SiC
[0027] According to the same method as in Example 1, the catalyst was used for oxidation reaction at 395° C. (hot spot). The conversion of isobutene was 94.9%, the selectivity of MAL was 89.8%, the selectivity of MAA was 1.2%, and the total yield of MAL and MAA was 86.4%.
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