Abstract

A thermal conversion of biomass to hythane using catalysts was studied. Low-temperature pyrolysis of two different types of biomass was performed in a pressure sealed reactor, and the resulting gas with high contents of CO2 and CO was methanized in a hydrogen atmosphere at a pressure of 30 bar. As catalysts, Ni/Al2O3, NiCo/Al2O3 and NiMo/Al2O3 were used and their catalytic activity was evaluated. The NiCo/Al2O3 catalyst showed the highest catalytic activity, Ni/Al2O3 had a lower but comparable one, and NiMo/Al2O3 showed the lowest activity. The resulting hythane contained 70 vol.% CH4 and 10 vol.% H2 (with NiCo/Al2O3 catalyst, HHV 29.20 MJ/m3, LHV 26.32 MJ/m3), or 57 vol.% CH4 and 23 vol% H2 (with Ni/Al2O3, HHV 25.92 MJ/m3, LHV 23.21 MJ/m3) or 47 vol.% CH4 and 27 vol.% H2 (with NiMo/Al2O3, HHV 23.23 MJ/m3, LHV 20.76 MJ/m3). It has been found that secondary reactions of volatile biomass products are of great importance for successful pressure pyrolysis.

Highlights

  • Biomass is an important source of renewable energy

  • Two contrasting types of biomass have been selected for the experiments: birch-wood shavings and ground apricot stones

  • The reason is that the efficiency of catalysts should first be tested on biomass samples with a completely different composition and only after identifying the influence of the catalysts and their compositions, it is possible to proceed to systematic experiments with a wider spectrum of biomass

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Summary

Introduction

The possibilities of its conversion using non-combustion technologies into further utilizable, energy-rich products (bio-oils, solid carbonaceous residues and energy gases) are far from being explored. Bio-oil can be utilized as a clean fuel and as a source of commercially useful chemicals, whereas biochar can be used as a smokeless fuel, and alternatively as a fertilizer or sorbent. Depending on the method of thermal treatment and the type of biomass, the gas may contain predominantly CO2 and CO and can be a source of these gases in the production of synthetic methane by the Power-to-Gas technology [3], designed on the basis of the Sabatier reaction [4,5]. If the methane content in the resulting gas is higher, e.g., 20–30 vol.%, it is possible to consider its subsequent conversion to hythane, in our case in the presence of a catalyst

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