Ceria-zirconia supported Pt-Fe bimetallic catalyst for water gas shift reaction with suppressed methanation activity in reformate-simulated gas

IF 3.9 2区 化学 Q2 CHEMISTRY, PHYSICAL
A.M. Gorlova , A.A. Saraev , V.N. Rogozhnikov , P.V. Snytnikov , D.I. Potemkin
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引用次数: 0

Abstract

PtFe/Ce0.75Zr0.25O2 catalysts were prepared using deposition and impregnation techniques and tested in water gas shift reaction in reformate-simulated feed gas. For the catalyst prepared by subsequent deposition of the metals it was observed that iron (mole ratio Pt:Fe ≈ 1.5) provides for inhibition of side reaction of methanation at the temperatures up to 350 °C. The water gas shift reaction rate per Pt surface area was also increased compared to the catalyst without iron (Pt content was the same). XPS analysis of PtFe/Ce0.75Zr0.25O2 showed that there are Pt0 and Fe2+ cations on the surface in H2 atmosphere at 150–350 °C. In situ DRIFTS results demonstrated stronger CO adsorption on the Pt-support interfacial sites and higher CO2 formation rate in the gas phase going from Pt to Pt-Fe system.
二氧化锆负载Pt-Fe双金属催化剂在重整模拟气体中抑制甲烷化活性的水煤气转移反应
采用沉积和浸渍技术制备了PtFe/Ce0.75Zr0.25O2催化剂,并在重整炉模拟原料气中进行了水煤气变换反应试验。对于随后沉积金属制备的催化剂,观察到铁(摩尔比Pt:Fe≈1.5)在高达350℃的温度下具有抑制甲烷化副反应的作用。与不含铁(Pt含量相同)的催化剂相比,每Pt表面积的水煤气转移反应速率也有所提高。对PtFe/Ce0.75Zr0.25O2的XPS分析表明,在150 ~ 350℃的H2气氛中,PtFe/Ce0.75Zr0.25O2表面存在Pt0和Fe2+阳离子。原位漂移结果表明,在Pt-载体界面位置上CO吸附更强,并且从Pt到Pt- fe体系的气相中CO2形成速率更高。
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来源期刊
Molecular Catalysis
Molecular Catalysis Chemical Engineering-Process Chemistry and Technology
CiteScore
6.90
自引率
10.90%
发文量
700
审稿时长
40 days
期刊介绍: Molecular Catalysis publishes full papers that are original, rigorous, and scholarly contributions examining the molecular and atomic aspects of catalytic activation and reaction mechanisms. The fields covered are: Heterogeneous catalysis including immobilized molecular catalysts Homogeneous catalysis including organocatalysis, organometallic catalysis and biocatalysis Photo- and electrochemistry Theoretical aspects of catalysis analyzed by computational methods
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