Supported propane dehydrogenation catalyst and preparation method thereof
A technology for propane dehydrogenation and catalyst, which is used in catalyst activation/preparation, dehydrogenation to hydrocarbons, chemical instruments and methods, etc. Effect
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Embodiment 1
[0052] (1) Weigh 10 grams of alumina carrier, add 20 ml of tartaric acid with a concentration of 0.74 g / mL and a saturated adsorption capacity (x / m) M of 0.6 as a competitive adsorbent, wherein the molar ratio of the carrier to the competitive adsorbent is 2.
[0053] (2) Fully impregnate the carrier with the above competitive adsorbent solution, the impregnation temperature is 10-50°C, and the impregnation time is 12-48 hours, so that the competitive adsorbent can fully enter the interior of the carrier.
[0054] (3) preparing 100 milliliters of concentrations is 2.1g / mL containing chromium nitrate, concentration is the solution of sodium nitrate and 0.18g / mL tin chloride of 0.07g / mL, the metal molar ratio ( sodium and tin) is 0.7.
[0055] (4) Quickly add the solution obtained in step (3) to the carrier in step (2), and then put it in an oven at 80°C, and quickly evaporate the excess water to dryness.
[0056] (5) The sample obtained in step (4) was calcined in a muffle fur...
Embodiment 2-7
[0058] Same as the examples, only different acidic species were changed as competing adsorbents.
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