Metal tungstates for use as nitrogen oxides reduction catalysts
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Preparation of MWO4
[0037]Starting materials of Co(NO3)2, MnCl2, Fecl2, Ni(NO3)2 or Cu(SO4)4 and Na2WO4.2H2O were purchased from Sigma-Aldrich and used directly without further purification. In a typical synthesis a (0.2M) Na2WO4 solution was combined with a (0.2M) transition metal solution in a stoichiometric manner with strong agitation. The solution mixture was then placed into a glass microwave tube. A microwave assisted hydrothermal synthesis was conducted on a microwave reactor (Anton Paar Microwave 300). The microwave tube was heated to various temperatures at max power (800 W). The exposure to microwaves was maintained for various times as will be discussed in more detail below. Following the exposure to microwaves the tube was cooled by forced air flow. The resulting product was rinsed with DI water multiple times on a centrifuge followed by vacuum drying overnight at 60 degrees C. Following the drying step, the catalyst material was calcined in air at 550 degrees C. for 60...
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Activity Testing MWO4
[0039]The activity testing was performed in a laboratory scale packed bed reactor (PID Eng&Tech Microactivity-Reference). Activity was determined for NO reduction by the hydrocarbon propylene (C3H6). Activity testing was performed under stoichiometric conditions both in oxygen deficient and oxygen rich conditions. As depicted in FIG. 3, under oxygen deficient conditions, the stoichiometric ratio of NO:C3H6 is 9:1, and under oxygen rich conditions, the stoichiometric ratio of NO:C3H6:O2 is 3:1:3. Also depicted in FIG. 3, 100 mg of catalyst material was combined with 400 mg of quartz sand and a total flowrate of 100 ml / min (gas hour space velocity GHSV˜15,000 inverse hours) was used for the testing in both oxygen rich and oxygen deficient conditions. A pretreatment phase includes heating the reactor and catalyst mixture to 500 degrees C. and maintaining the temperature for 15 minutes under oxidizing conditions (30 ml / min of 10% O2 in He balance). The reactor is t...
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