Recovery method of microspherical catalyst of fluid bed
A technology of catalyst and fluidized bed, which is applied in the recovery field of microsphere catalyst for fluidized bed
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Embodiment 1
[0021] According to the solid content of oxide dry basis in the material solution of 30wt%, the measured silica sol (content 30wt%), aluminum sol (content 20%), calcium nitrate (content 23%), kaolin (content 85wt%) and SAPO -34 molecular sieve raw powder was added to a certain amount of deionized water in sequence, stirred for 30 minutes (the oxide dry basis mass content of each raw material was 25%, 10%, 5%, 30%, 30% in sequence), and finally added Sesbania powder (soaked with a small amount of ethanol) equivalent to 0.5% of the total oxide dry basis mass, stirred for 30 min. The material liquid is passed through the colloid mill for colloid grinding, so that 70% of the particle diameter in the final slurry is less than 5 μm. After the slurry is placed at room temperature for 2 hours, it is subjected to centrifugal spray drying. The rotating speed of the atomizer is 30 Hz, the inlet temperature is 400°C, and the outlet temperature is not less than 120°C. The spray-dried produ...
Embodiment 2
[0023] The MC sample obtained in Example 1 was used in a circulating fluidized bed (catalyst loading capacity of 4 tons, methanol processing capacity of 50 tons / day) for an industrial test to perform methanol conversion to olefin reaction. Device level
[0024] After 30 days of stable operation, take out the collected catalyst powder from the sampling port of the cyclone separator and record it as XM. Take a small amount of catalyst sample from the sampling port of the reactor and record it as FM.
Embodiment 3
[0026] Take part of XM and FM samples, and roast them in air at 650°C to remove the moisture and reaction residual carbon contained in them. The samples obtained are denoted as XMC and FMC, respectively.
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