Catalyst for oxygen-containing compound conversion to produce olefine microshpere and preparing method thereof
A catalyst and a technology for producing olefins, which are used in the production of hydrocarbons from oxygen-containing organic compounds, metal/metal oxide/metal hydroxide catalysts, catalyst activation/preparation, etc., can solve problems such as no literature reports, and achieve suitable particle size Distribution, high wear index effect
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Embodiment 1
[0018] Embodiment 1 (silicon-phosphorus-aluminum system catalyst)
[0019] According to the calculation that the solid content of oxide dry basis in the feed liquid is 30wt%, the metered silica sol (content 30wt%), kaolin (content 85wt%) and SAPO-34 molecular sieve former powder are sequentially added to a certain amount of deionized water, Stir for 30min (the oxide dry basis mass content of each raw material is respectively 30%, 40%, and 30%) in sequence, and finally add the squash powder (soaked with a small amount of ethanol) equivalent to the total oxide dry basis mass of 0.25%, and stir 30min. The feed liquid is passed through a colloid mill for colloid milling, so that 70% of the particle diameters in the finally obtained slurry are less than 5 μm. After the slurry was left at room temperature for 2 h, pressure spray drying was carried out. The pressure of the pressure nozzle is 1MPa, the inlet temperature is 400°C, and the outlet temperature is not lower than 120°C. ...
Embodiment 2
[0020] Embodiment 2 (silicon-phosphorus-aluminum system catalyst)
[0021] According to the calculation that the dry basis solid content of the oxide in the feed liquid is 30wt%, the measured aluminum sol (content 20wt%), kaolin (content 85wt%) and SAPO-34 molecular sieve former powder are sequentially added to a certain amount of deionized water, and stirred 30min (the oxide dry basis mass content of each raw material is respectively 20%, 50%, 30%) in sequence, finally add the squash powder (soaked with a small amount of ethanol) that is equivalent to the total oxide dry basis mass 1%, and stir for 30min . The feed liquid is passed through a colloid mill so that 70% of the particle diameters in the finally obtained slurry are less than 5 μm. After the slurry was left at room temperature for 2 h, pressure spray drying was carried out. The pressure of the pressure nozzle is 1.5MPa, the inlet temperature is 400°C, and the outlet temperature is not lower than 120°C. The obtain...
Embodiment 3
[0022] Embodiment 3 (silicon-phosphorus-aluminum system catalyst)
[0023]Mix 1.69 kg of phosphoric acid (85 wt%) with 9 kg of deionized water and 2.95 kg of pseudo-boehmite (70 wt%), and stir for 30 minutes to form an aluminum phosphate gel. Mix 1.56kg SAPO-34 molecular sieve raw powder, 0.83kg silica sol (30% content) and 10kg deionized water, stir for 20min, and then add to the previous gel. The solid content of oxide dry basis in the feed liquid is 20wt% (the oxide dry basis mass content of each raw material is respectively 28.7%, 41.3%, 25%, 5%), and finally add 0.5% of the total oxide dry basis mass. % scallop powder (soaked with a small amount of ethanol), stirred for 30min. The feed liquid passes through the colloid mill so that 70% of the particle diameters in the finally obtained slurry are less than 5 μm. The slurry was subjected to centrifugal spray drying. The rotational speed of the centrifugal atomizer is 30Hz, the inlet temperature is 400°C, and the outlet t...
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