Zn-Co/HZSM-5 catalyst for eliminating nitroxide from methane product and its preparing method
A technology of nitrogen oxides and HZSM-5, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of only 34% maximum conversion rate, narrow active temperature range, and ineffective effects, etc. , to achieve the effect of simple preparation method, improved efficiency and obvious effect
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Embodiment 1
[0018] Catalyst of the present invention uses cobalt and zinc as active component, is loaded on the artificially synthesized silicon-aluminum ratio and is on the HZSM-5 of 25, and the weight percent of cobalt carried on the molecular sieve is 2%, and the weight percent of zinc is 2%, namely: Zn-Co / HZSM-5 (1:1:50);
[0019] Now take the Zn-Co / HZSM-5 catalyst (silicon-aluminum ratio is 25) that contains Zn2%, Co2% (percentage by weight) as an example to generally describe the preparation of the catalyst used in the present invention, specifically: adopt Cobalt nitrate and zinc nitrate configuration containing Zn 2+ and Co 2+ A solution of 2% (percentage by weight) is used as the impregnation solution. Take 2ml of the solution and impregnate it on 2 grams of HZSM-5 molecular sieve, heat and stir at 80°C for 6 hours, let it stand for 24 hours, and bake it at 120°C for 3 hours. Put it in a muffle furnace and bake at 700°C for 6 hours. Finally, the catalyst is pressed into tablets...
Embodiment 2
[0035] The preparation of embodiment 2Zn-Co / HZSM-5 (1: 2.5: 50) catalyst
[0036] The difference from Example 1 is that the impregnation solution contains Co 2+ 5%, containing Zn 2+ 2% solution, Zn-Co / HZSM-5 (1: 2.5: 50) catalyst was prepared in the same manner as in Example 1.
Embodiment 3
[0039] Example 3. Activity test of catalyst in the selective reduction of nitric oxide by methane under oxygen-enriched conditions
[0040] Activity tests were performed in a fixed bed reactor. Before entering the reactor, nitrogen monoxide, methane, oxygen and helium are fully mixed in the mixer, the amount of catalyst used in the activity test is 0.8ml, the inner diameter of the reactor is 10mm, and the space velocity GHSV of the raw material gas is 3600h -1 , the reaction pressure is normal pressure, the reactor is placed in a temperature-controlled electric furnace, and the reaction temperature is 350-600°C. The reaction product was analyzed by on-line chromatography, and the catalyst activity was measured by the conversion rate (%) of nitric oxide into nitrogen.
[0041] Test result analysis example 1
[0042] Table 1 lists the catalytic activity test comparison of the catalysts prepared in Comparative Examples 1 and 2 and Example 1 according to Example 3. It can be see...
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