2013
DOI: 10.1016/j.jiec.2013.01.012
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Water-gas shift reaction over Cu–Zn, Cu–Fe, and Cu–Zn–Fe composite-oxide catalysts prepared by urea-nitrate combustion

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Cited by 20 publications
(12 citation statements)
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“…Similar trends were observed for the dependence of the CO consumption rate and Cu 0 surface areas on the CuO/CuAl 2 O 4 ratios (Figure 9), showing a strong positive correlation between the Cu 0 surface area and the WGS reaction rate. The CO consumption rate was calculated using the following These results (Figure 9) further support the conclusions of earlier studies that Cu 0 is the active surface site responsible for the WGS activity of Cu−Pd/γ-Al 2 O 3 catalysts, as it is the proposed WGS active sites of Cu−Ni/Al 2 O 3 , 22 Cu−Fe/ Al 2 O 3 , 48 Cu−ZnO/Al 2 O 3 , 49 and Cu−MgO/Al 2 O 3 . 50 The volcano plots shown in Figure 9 suggest that CuAl 2 O 4 formation may result in an additional Cu 0 surface area for up to the molar CuO/CuAl 2 O 4 = 2.37 (CuPd2), but excessive CuAl 2 O 4 formation reduced Cu 0 surface area and therefore the WGS activity.…”
Section: Resultssupporting
confidence: 80%
“…Similar trends were observed for the dependence of the CO consumption rate and Cu 0 surface areas on the CuO/CuAl 2 O 4 ratios (Figure 9), showing a strong positive correlation between the Cu 0 surface area and the WGS reaction rate. The CO consumption rate was calculated using the following These results (Figure 9) further support the conclusions of earlier studies that Cu 0 is the active surface site responsible for the WGS activity of Cu−Pd/γ-Al 2 O 3 catalysts, as it is the proposed WGS active sites of Cu−Ni/Al 2 O 3 , 22 Cu−Fe/ Al 2 O 3 , 48 Cu−ZnO/Al 2 O 3 , 49 and Cu−MgO/Al 2 O 3 . 50 The volcano plots shown in Figure 9 suggest that CuAl 2 O 4 formation may result in an additional Cu 0 surface area for up to the molar CuO/CuAl 2 O 4 = 2.37 (CuPd2), but excessive CuAl 2 O 4 formation reduced Cu 0 surface area and therefore the WGS activity.…”
Section: Resultssupporting
confidence: 80%
“…In recent years, there has been a renewed interest in the WGS reaction due to the tremendous growth in fuel cell technology and the need to develop small-scale fuel processors [5,6]. However, conventional high temperature (Fe 3 O 4 /Cr 2 O 3 ) and low temperature (Cu/ZnO/ Al 2 O 3 ) WGS catalysts cannot be used in those applications and thereby many researches are focused on the development of active, stable, and cost effective WGS catalysts [7][8][9][10][11][12][13][14].…”
Section: Introductionmentioning
confidence: 99%
“…1) is known as a prominent reaction with various uses in ammonia synthesis, pure hydrogen production, and recently fuel-cell technology [1][2][3][4][5][6][7][8][9][10][11][12]. This reaction is usually run in two steps: a high-temperature shift (HTS, 350-500°C, over Fe-Cr-based catalysts) [13][14][15] and a low-temperature shift (LTS, 150-300°C, over Cu-Zn-based catalysts) [5,13].…”
Section: Introductionmentioning
confidence: 99%