Studies of the role of the copper promoter in the iron oxide/chromia high temperature water gas shift catalyst

A study of the role of the copper promoter in the iron oxide/chromia high temperature water gas shift reaction is reported and discussed. The rate of reaction using both CuO/Fe3O4/Cr2O3 and Fe3O4/Cr2O3 catalysts is zero order in H2O and first order in CO over a wide range of reactant compositions and reaction pressures. The activation energy for the Fe3O4/Cr2O3 catalyst is found to be 118±9 kJ mol−1 which is in agreement with previous literature data. The addition of CuO to the Fe3O4/Cr2O3 catalyst significantly decreases the activation energy to ca. 75–80 kJ mol−1. TPR studies using H2/He and H2/CO indicate that the addition of CuO partially stabilises the catalyst with respect to reduction with CO, indicating that one role of CuO as a promoter is to permit the use of higher partial pressures of CO in the reactant gases. Model experiments with CH3OH/CO mixtures show that the addition of CuO to the Fe3O4/Cr2O3 catalyst promotes the formation of methyl formate significantly. Based on these findings, the possible role of CuO in the promoted catalyst is discussed.

[1]  M. C. Rangel,et al.  Effect of chromium on magnetite formation , 1995 .

[2]  C. Rhodes,et al.  Water-gas shift reaction: finding the mechanistic boundary , 1995 .

[3]  T. Salmi,et al.  A dynamic study of the water-gas shift reaction over an industrial ferrochrome catalyst , 1988 .

[4]  G. Chinchen,et al.  A comparison of the water-gas shift reaction on chromia-promoted magnetite and on supported copper catalysts , 1988 .

[5]  V. Idakiev,et al.  Effect of copper oxide on the catalytic activity of iron-chromia catalyst for water gas shift reaction , 1987 .

[6]  J. Dumesic,et al.  The effects of metal-oxygen bond strength on properties of oxides: II. Water-gas shift over bulk oxides , 1986 .

[7]  P. Ford The water gas shift reaction: homogeneous catalysis by ruthenium and other metal carbonyls , 1981 .

[8]  M. Boudart,et al.  Mössbauer spectroscopy of CO shift catalysts promoted with lead , 1973 .

[9]  Douglas M. Ruthven,et al.  The activity of commercial water gas shift catalysts , 1969 .

[10]  G. Hutchings,et al.  Cobalt–manganese oxide water-gas shift catalysts. A kinetic and mechanistic study , 1989 .

[11]  J. Dumesic,et al.  Isotopic exchange measurements of the rates of adsorption/desorption and interconversion of CO and CO2 over chromia-promoted magnetite: implications for water-gas shift , 1987 .

[12]  J. Dumesic,et al.  Water-gas shift over magnetite particles supported on graphite: Effects of treatments in CO/CO2 and H2/H2O gas mixtures , 1985 .

[13]  G. Chinchen,et al.  Water-gas shift reaction over an iron oxide/chromium oxide catalyst. , 1984 .

[14]  G. Chinchen,et al.  Water-gas shift reaction over an iron oxide/chromium oxide catalyst.: II: Stability of activity , 1984 .

[15]  G. Chinchen,et al.  Water-gas shift reaction over an iron oxide/chromium oxide catalyst.: III: kinetics of reaction , 1984 .

[16]  D. Newsome The Water-Gas Shift Reaction , 1980 .

[17]  P. Fott,et al.  Kinetics of the carbon monoxide conversion with steam at elevated pressures , 1979 .

[18]  R. Sherwood,et al.  Magnetic properties and site distributions in the system FeCr2O4-Fe3O4(Fe2+Cr2−xFex3+O4 , 1971 .

[19]  H. Flood,et al.  The Kinetics of the Water Gas Conversion. II. Investigations at Elevated Pressures. , 1962 .

[20]  Norman C. Li,et al.  The Kinetics of the Water Gas Conversion at Atmospheric Pressure. , 1961 .