Ammonia scr catalyst and method of using the catalyst
A catalyst, ammonia source technology, applied in molecular sieve catalysts, chemical instruments and methods, catalyst activation/preparation, etc., can solve public health problems and other issues
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Embodiment 1
[0148] Synergy between manganese first component and cerium second component
[0149] Catalysts with the compositions shown in Table 1 were prepared and tested for ammonia SCR reduction of nitrogen oxides. The weight percents of manganese and cerium are given on an oxide and metal basis, respectively, with metal-based weight percents placed in parentheses in the table.
[0150] Table 1
[0151] Composition of Mn and Ce catalysts
[0152]
[0153] Zeolite and OSM were placed on the substrate as an eluting coating at a loading of about 150 g / L. The eluate coating was dried at room temperature and then calcined at 550 °C for 4 hours. The aqueous solutions of manganese nitrate and cerium nitrate are combined and dipped into the stripped coating on the substrate. The catalyst was dried and calcined at 550 °C for 2 hours. The OSM contains the formula Ce 0.24 Zr 0.66 La 0.04 Y 0.06 o 2 CZLY, and the zeolite consists of ZSM-5.
[0154] The catalysts in Table 1 were teste...
Embodiment 2
[0161] NO and NO / N0 2 Effect of Feed Gas on the Activity of Iron β-SCR
[0162] Iron-exchanged zeolite beta was supplied by Tricat GmbH, Bitterfeld, Germany. Catalyst 4 having the composition shown in Table 2 was prepared from iron-exchanged Beta zeolite.
[0163] Table 2
[0164] Composition of iron-exchanged β catalyst
[0165] Catalyst No.
wt% iron exchanged beta zeolite
wt % OSM
4
50
50
[0166] Catalyst 4 was tested with two different feed gases as fresh catalyst and after hydrothermal aging. The first feed gas contains 350ppm NO, no NO 2 . The second feed gas contains 175ppm NO and 175ppm NO 2 mixture. NO / NO of two feed gases x The graph of conversion rate versus temperature is shown in figure 2 shown.
[0167] Mixed NO / NO 2 For feed gas or feed gas containing only NO, hydrothermal aging has little effect on the activity of Catalyst 4.
[0168] Activity of fresh and hydrothermally aged Catalyst 4 for NO containing bu...
Embodiment 3
[0170] NO and NO / N0 2 Effect of Feed Gas on Activity of Mn / Ce / Zeolite / OSM Catalyst
[0171] In Example 3, with NO and NO / NO 2 The feed stream was tested for SCR activity of Catalyst 3, which is a Mn / Ce / Zeolite / OSM catalyst, a catalyst according to an embodiment of the present invention. The catalyst was tested as fresh catalyst and after hydrothermal aging. The result is as image 3 as shown.
[0172] Fresh and hydrothermally aged catalyst 3 for mixed NO / NO 2 Feed gas NO x The transforming activities were essentially the same.
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