Monolithic cordierite carrier hydrodechlorination catalyst and preparation method and application thereof
A kind of technology of hydrodechlorination, cordierite
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preparation example
[0057]Preparation of monitrous doped carbon coated integrated cordierite carrier:
[0058]Starch, glucose, ethylenediamine and water are equipped with aqueous solution by 1: 2: 2: 2, and immerse the integral cordierite carrier, uniformly coated with the surface of the integral cordierite carrier, 110 ° C After drying for 3 hours, it was placed in a nitrogen atmosphere and fed at 400 ° C for 5 hours. Under the same conditions, the impregnation coating was continued, dried, and baked. After three coating, drying and calcined, nitrogen-doped-coated integrated cordierite carrier, the specific surface area of the nitrogen-doped carbon coated integrated cordierite carrier is 1270m2 / g, the carbon coating content is 4.0 wt%, of which the nitrogen content is 5.0% by weight.
[0059]Change the coating conditions of the nitrogen doped carbon coating, obtain an integrated cordierite carrier which is different from surface area, carbon content, and nitrogen content, as shown in Table 1 below:
[0060]...
Embodiment 1
[0064]Preparation of hydrocarbon chlorine catalyst:
[0065]S1. Active Metal Load: The above-mentioned prepared nitrogen-doped carbonate 1 is rinsed with deionized water, immersed in aqueous chloride solution, and the palladium content is 0.08 of the integrated cordierite carrier. %, The total volume of the impregnation liquid and the volume ratio of the integral cordierite carrier is 2: 1. The stirring was turned on, warmed to 50 ° C, and removed after 3 hours; at 30 ° C, the air humidity was allowed to stand for 15 hours, then the flow rate was 0.5 m / s nitrogen stream (containing 0.1V / V oxygen) Scan for 1 hour.
[0066]S2. Second Metal Load: 1) Active Metal Ion Restore: The integral cordierite carrier of the load-shaped active metal with a nitrogen flow is placed in a high pressure reactor, immersed in the ethylene glycol solution, and the bottom of the kettle The child is used for stirring (revolutions 1500R / min), continuously venting hydrogen in the ethylene glycol solution, war...
Embodiment 2
[0072]The operation of the present embodiment is in the same embodiment, and the difference is only that the carrier 3 is used instead of the carrier 1 for the preparation of the hydrodechlorination catalyst, the active metal load is 0.8%, the second metal load is reduced to 1.5%, and the prepared obtained The catalyst is recorded as CAT2.
[0073]The TEM is characterized, 93% of the active metal particles in the CAT2 are in a wrap type bimetal structure.
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