Alkane dehydrogenation catalyst and preparation method thereof
A dehydrogenation catalyst, catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of low propane conversion rate, shortened catalyst life, etc., To achieve the effect of simple preparation method, inhibiting carbon deposition and improving activity stability
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example 1
[0016] Weigh commercially available alumina carrier (spherical, diameter 0.5mm, pore volume 0.71cm3 / g, specific surface area 224m 2 / g, the carrier used in the following examples) 30g, deionized water was added dropwise to initial moistening, and the volume of consumed water was 27mL. Assuming that the Sn content accounted for 3wt% of the final catalyst, tin tetrachloride containing 0.9g of Sn was weighed and dissolved in deionized water, and the volume was adjusted to 27mL. Add the prepared Sn-containing solution into 30g of alumina carrier, mix well, and age for 2h. Dry at 80°C for 8 hours, then bake at 600°C for 4 hours. After roasting, the sample is placed in a rotary evaporator for vacuum treatment at a temperature of 70°C, and the vacuum degree is controlled below 10kPa. After 1 hour of treatment, the temperature is lowered, and 100mL of methanol is added to return to normal pressure, heated to reflux, the heating temperature is 55°C, and the treatment time is 4 hours. ...
example 2
[0019] The ethanol-treated catalyst was prepared according to the process described in Example 1, and the content of each component in the catalyst obtained at a reflux temperature of 70°C was: Pt 0.6 wt%, Sn 3.0 wt%, Na 1.0 wt%. The resulting catalyst is designated C-2.
example 3
[0021] According to the process described in Example 1, the catalyst was treated with methanol and ethanol mixed solvent. The molar ratio of methanol and ethanol was 1:3, and the reflux temperature was 66°C. The content of each component in the prepared catalyst was: Pt 0.6wt%, Sn3. 0 wt%, Na 1.0 wt%. The resulting catalyst is designated C-3.
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