Alumina-based lean NOx trap system and method of use
a technology of nox traps and nox, which is applied in the direction of separation processes, machines/engines, mechanical equipment, etc., can solve the problems of loss of both catalyst activity, low efficiency, and low durability of conventional nox traps, and achieve efficient desulphurization and extended use
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example 1
[0067] An alumina-based lean NOx trap (LNT) was prepared in accordance with the present invention using only Pt as the catalyst and was exposed to synthetic exhaust gas at temperatures ranging from about 1000 to 450° C. The composition of synthetic exhaust gas used in the LNT laboratory tests is listed in Table 1 below.
TABLE 1Gases used in LNT Lab TestGasLeanRichCO500 ppm4%H2167 ppm1.33%C3H6300 ppm C15000 ppm C1NOx500 ppm500 ppmO210%1%CO25%5%H2O5%5%λ = 2.0λ = 0.90
FIG. 6 illustrates the resulting NOx conversion efficiency under varying conditions in a lean / rich cycle of 24 sec. / 6 sec. The conditions for the alumina-based LNT included operation under lean conditions at 700° C. for 20 minutes, and an additional 10 minutes under rich conditions at 350° C. As can be seen, the fresh alumina LNT exhibits good NOx conversion efficiency at low temperatures, but the 700° C. lean treatment causes the NOx activity to deteriorate. The rich treatment at 350° C. does not restore the activity.
example 2
[0068] An alumina-based LNT was prepared in accordance with the present invention using both Pt and Rh as catalysts. The trap was exposed to exhaust gas at temperatures ranging from about 100 to 450° C. FIG. 7 illustrates the NOx conversion efficiency under varying conditions in a lean / rich cycle of 24 s / 6 s. The conditions for the alumina-based LNT included operation under lean conditions at 700° C. for 20 minutes and an additional 10 minutes under rich conditions at 350° C.
[0069] As can be seen, the fresh alumina-based LNT has good NOx conversion efficiency at low temperatures, and the 700° C. lean treatment causes the NOx activity to deteriorate, but the rich treatment at 350° C. largely restores the activity. It can be concluded that the combination of Pt and Rh catalysts is preferred for use in the alumina-based LNT of the present invention.
[0070]FIG. 8 illustrates the NOx storage capacities of the alumina-based LNTs of the present invention, with either pure alumina or alumi...
example 3
[0075] An alumina-based LNT was prepared in accordance with the present invention using both Pt and Rh as catalysts and was exposed to 30 ppm SO2 at 200° C. to 450° C. and λ=2.0 for 3200 seconds. A desulphurization (de-SOx) treatment was then performed at 650° C. under slightly rich conditions. FIG. 11 illustrates the de-SOx process of the alumina LNT at 650° C. and λ=0.987. The sulfur loading was 1.14 g per liter and the desulphurization started at t=5500 seconds. More than 95% by weight of the sulfur was released in about 60 seconds as SO2. Similar efficient desulphurization properties were shown when the alumina-based LNT was modified by a very small amount (less than 2.0 wt %) of calcium oxide through solution ion exchange as shown in FIG. 12.
[0076]FIG. 13 compares the de-SOx performance of the alumina-based LNT of the present invention with a conventional LNT comprised of Ba oxide supported on alumina as the NOx storage material with similar sulfur loading (1.14 g / liter). The ...
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