Catalytic performance of Co-Mo-Ce-K/γ-Al2O3 catalyst for the shift reaction of CO in coke oven gas

Yuqiong ZHAO , Yongfa ZHANG

Front. Chem. Sci. Eng. ›› 2010, Vol. 4 ›› Issue (4) : 457 -460.

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Front. Chem. Sci. Eng. ›› 2010, Vol. 4 ›› Issue (4) : 457 -460. DOI: 10.1007/s11705-010-0524-7
RESEARCH ARTICLE
RESEARCH ARTICLE

Catalytic performance of Co-Mo-Ce-K/γ-Al2O3 catalyst for the shift reaction of CO in coke oven gas

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Abstract

The catalytic performance of Co-Mo-Ce-K/γ-Al2O3 catalyst for the shift reaction of CO in coke oven gas is investigated using X-ray diffraction (XRD) and temperature-programmed reduction (TPR). The results indicate that Ce and K have a synergistic effect on promoting the catalytic activity, and the Co-Mo-Ce-K/γ-Al2O3 catalyst with 3.0 wt-% CeO2 and 6.0 wt-% K2O exhibits the highest activity. CeO2 favors Co dispersion and mainly produces an electronic effect. TPR characterization results indicate that the addition of CeO2-K2O in the Co-Mo-Ce-K/γ-Al2O3 catalyst decreases the reduction temperature of active components, and part of octahedrally coordinated Mo6+ transforms into tetrahedrally coordinated Mo6+, which has a close relationship with the catalytic activity.

Keywords

coke oven gas / water gas shift reaction / sulfur-tolerant catalyst / cerium dioxide

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Yuqiong ZHAO, Yongfa ZHANG. Catalytic performance of Co-Mo-Ce-K/γ-Al2O3 catalyst for the shift reaction of CO in coke oven gas. Front. Chem. Sci. Eng., 2010, 4(4): 457-460 DOI:10.1007/s11705-010-0524-7

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