High-activity propylene gas-phase epoxidation catalyst and preparation method thereof
A catalyst and high-activity technology, applied in the direction of heterogeneous catalyst chemical elements, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low PO yield and achieve cost and The effect of less environmental pollution and easy industrialization
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Embodiment 1
[0019] Example 1: Bi 2 SiO 5 Synthesis of nanosheets: Weigh 200 mmol of bismuth nitrate and dissolve in 1000 ml of ethylene glycol-glycerol-water mixed solution, and stir for 1 h, then weigh 100 mmol of tetraethyl orthosilicate and dissolve in ethanol solution and added dropwise to the above solution, continued to stir for 1 h, then added 1000 ml of deionized water; then adjusted the pH to 9 with 28% ammonia water, and then transferred the obtained white emulsion to a 180 °C oven for crystallization for 12 h , followed by centrifugation and washing to pH = 7, the obtained white solid was dried at 70 °C for 10 h, and the obtained sample was ground and calcined at 500 °C for 4 h to obtain the carrier nanosheet Bi 2 SiO 5 .
[0020] Catalyst Fe 2 o 3 -MoO 3 -Bi 2 SiO 5(Molar ratio Si / Bi=0.5, Mo / Bi=0.15, Fe / Mo=0.3) preparation: weigh 50 g of the above Bi 2 SiO 5 The nanosheets were dispersed in 500 ml of deionized water and stirred in an ice-water bath for 0.5 h; Mo / Bi=0...
Embodiment 2
[0022] Example 2: The catalyst system as in Example 1, but using sodium silicate as the silicon source and bismuth chloride as the bismuth source, crystallized at 140 °C for 4 h, and dried the resulting white solid at 110 °C for 4 h to prepare Bi 2 SiO 5 Nanosheets, according to the molar ratio of Mo / Bi=0.02, Fe / Mo=0.06 to prepare catalyst Fe 2 o 3 -MoO 3 -Bi 2 SiO 5 The stirring condition when loading the active components was stirring in an ice-water bath for 3 h, the obtained sample was dried at 70 °C for 4 h, ground and roasted at 450 °C for 20 h, other reaction conditions were the same as in Example 1. The results of the epoxidation reaction are shown in Table 1.
Embodiment 3
[0023] Embodiment 3: as the catalyst system of embodiment 1, but prepare Fe according to the ratio of molar ratio Si / Bi=0.1, Mo / Bi=0.3, Fe / Mo=0.5 2 o 3 -MoO 3 -Bi 2 SiO 5 , when the active component is loaded, ammonium molybdate is used as the molybdenum precursor and the stirring condition is stirring in an ice-water bath for 5 h, and the ultrasonic impregnation condition is ultrasonic vibration impregnation for 3 h, and the slurry obtained after stirring is dried at 180 °C for 3 h, and the particles are ground Then baked at 550 °C for 5 h. When evaluating the epoxidation activity, the reaction temperature is 400 °C, the pressure is 0.15 MPa, and the reaction temperature is 0.15 MPa. 2 O is the source of oxygen, N 2 O purity is greater than 99.9%, Fujian Xinhang Industrial Gas Co., Ltd., and other reaction conditions are the same as embodiment 1. The results of the epoxidation reaction are shown in Table 1.
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