Abstract

Fe-Ni and Co-Fe-Ni catalysts were prepared by the wet impregnation method for the production of high-calorific synthetic natural gas. The influence of Ni addition to Fe and Co-Fe catalyst structure and catalytic performance was investigated. The results show that the increasing of Ni amount in Fe-Ni and Co-Fe-Ni catalysts increased the formation of Ni-Fe alloy. In addition, the addition of nickel to the Fe and Co-Fe catalysts could promote the dispersion of metal and decrease the reduction temperature. Consequently, the Fe-Ni and Co-Fe-Ni catalysts exhibited higher CO conversion compared to Fe and Co-Fe catalysts. A higher Ni amount in the catalysts could increase C1–C4 hydrocarbon production and reduce the byproducts (C5+ and CO2). Among the catalysts, the 5Co-15Fe-5Ni/γ-Al2O3 catalyst affords a high light hydrocarbon yield (51.7% CH4 and 21.8% C2–C4) with a low byproduct yield (14.1% C5+ and 12.1% CO2).

Highlights

  • In the past decades, energy consumption has grown rapidly because of population growth

  • The increasing consumption of fossil fuels leads to the emission of greenhouse gases, carbon dioxide (CO2 ), which contribute to global warming

  • Synthetic natural gas (SNG; CO + 3H2 = CH4 + H2 O) production from biomass has been considered a substitute for fossil fuels, due to its high energy density and low greenhouse gas emission

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Summary

Introduction

Energy consumption has grown rapidly because of population growth Fossil fuels such as coal, petroleum, and natural gas are the main energy sources. Synthetic natural gas (SNG; CO + 3H2 = CH4 + H2 O) production from biomass has been considered a substitute for fossil fuels, due to its high energy density and low greenhouse gas emission. It can be transported efficiently using existing and widely distributed gas pipelines [1,2,3,4,5]. This has a problem that the heating value is lower than the standard heating value (10,400 kcal/Nm3 ) for power generation in South Korea and Japan

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