Nontoxic rare-earth denitration catalyst and preparation method and application thereof
A denitration catalyst and catalyst technology, which are applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems that the catalyst cannot have a stepped pore structure system, rarely reported solutions, and reduce catalytic activity. Achieve protection and catalytic performance, overcome insufficient conversion activity, and improve catalytic performance
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Embodiment 1
[0040] Will be taken from the deactivation of a local oil refinery in Shandong and unload the spent oil refinery catalyst (deoiled), and 250 grams of rare earth type catalytic cracking spent catalyst (FCC cerium-rich type anti-vanadium agent, CeO 2 4%, alumina ≥ 45%) and 250 grams of tungsten-containing hydrodenitrogenation refined waste catalyst (WO 3 22%, macroporous alumina ≥ 70%), crushed, ball milled, and passed through a 60-mesh sieve, mixed with 100 grams of high-alumina cement (industrial products, alumina ≥ 50%, Beijing Aoming Technology Co., Ltd.), 20 grams Corn starch (industrial product, moisture ≤ 11%, Nanjing Hanying Chemical Co., Ltd.), add deionized water and knead in a kneader. The water / powder weight ratio of the material is about 0.3:1. After kneading, it is extruded into a honeycomb shape The green body is cured at room temperature of 25° C. for 24 hours to become a silicon and aluminum oxide honeycomb green body containing rare earth and tungsten.
[00...
Embodiment 2
[0052] The molybdenum-containing hydrodesulfurization spent catalyst (MoO 3 13%, macroporous alumina ≥ 70%) 250 grams, replace the hydrodenitrogenation refining waste catalyst containing tungsten in embodiment 1, other preparation contents and steps are identical with embodiment 1, obtain the catalyzer of embodiment 2.
Embodiment 3
[0054] Get 200 grams of manganese acetate (chemically pure, ≥95%, Beijing Chemical Reagent Company), replace 140 grams of zirconium oxychloride in embodiment 1, other preparation content and steps are identical with embodiment 1, obtain the catalyst of embodiment 3.
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