Palladium-copper lightweight monolithic catalyst and preparation method and application thereof
A monolithic catalyst, palladium-copper technology, used in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc. The effect of cutting and folding
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Embodiment 1
[0019] After wetting 0.5 g of palladium copper / alumina catalyst with an appropriate amount of ethanol, it was dispersed in 4.5 mL of deionized water. Add 0.5 mL of styrene-acrylic emulsion dropwise to the above suspension, and stir at room temperature for 1 h to obtain an active slurry. Brush the active slurry evenly on the 100*150mm melt-blown cloth, and dry it in a blast drying oven at 70°C.
[0020] Catalyst evaluation: the feed gas component is, CO 20 ppm; the volume space velocity is 10000 h -1 ; Reaction temperature 30°C. Product analysis was performed using a carbon monoxide analyzer (Thermo, Model 48i) with a minimum detection limit of 0.04 ppm.
[0021] Test result, at 10000h -1 Under the volume space velocity, the initial CO purification rate of the obtained monolithic catalyst was 76%, and the activity did not decrease significantly after 24 hours.
Embodiment 2
[0023] After wetting 0.5 g of palladium copper / alumina catalyst with an appropriate amount of ethanol, it was dispersed in 4.5 mL of deionized water. Add 0.3 mL of styrene-acrylic emulsion dropwise to the above suspension, and stir at room temperature for 1 h to obtain an active slurry. Brush the active slurry evenly on the 100*150mm melt-blown cloth, and dry it in a blast drying oven at 70°C.
[0024] Catalyst evaluation is the same as embodiment 1, test result, at 10000h -1 Under the volume space velocity, the obtained monolithic catalyst had an initial CO purification rate of 90%, and the activity did not decrease significantly after 24 hours.
Embodiment 3
[0026] After wetting 0.5 g of palladium copper / alumina catalyst with an appropriate amount of ethanol, it was dispersed in 4.5 mL of deionized water. Add 0.8 mL of styrene-acrylic emulsion dropwise to the above suspension, and stir at room temperature for 1 h to obtain an active slurry. Brush the active slurry evenly on the 100*150mm melt-blown cloth, and dry it in a blast drying oven at 70°C.
[0027] Catalyst evaluation is the same as embodiment 1, test result, at 10000h -1 Under the volume space velocity, the initial CO purification rate of the obtained monolithic catalyst was 35%, and the activity did not decrease significantly after 24 hours.
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