Abstract

The ignition and combustion of anthracite modified by the addition of pyrolysis oil obtained during thermal processing of waste car tires (WCTs) had been studied. The mass fraction of WCT pyrolysis oil was varied in the range from 5 to 30 wt %. The additive was applied by the drop impregnation method. Ignition and combustion of obtained samples were carried out in a combustion chamber at temperatures of the heating medium Tg = 600–800 °C. The gas-phase combustion products were analyzed using an in-line gas analyzer. The application of WCT pyrolysis oil as a combustion modifier contributed to an increase in the reactivity of anthracite, which was expressed in a decrease in the minimum ignition temperature (by 23–104 °C) and a reduction in the ignition delay time. The high-speed video recording indicated that the combustion of both initial and modified with 5 wt % pyrolysis oil anthracite samples was realized in oxidation mode. For samples with more than 10 wt % pyrolysis oil additive, the formation of a visible flame was observed near the sample surface. With an increase in the mass fraction of the additive, the rate of combustion front propagation was increased. The application of WCT pyrolysis oil as a combustion modifier also contributed to the reduction or even the almost complete elimination of unburnt carbon content in the ash residue formed after anthracite combustion.

Highlights

  • Coal is one of the main fuels for power generation worldwide.[1]

  • Note that the addition of 5−15 wt % pyrolysis oil at Tg = 600 °C initiated the ignition of anthracite, which was shown by the decrease in ti value by 25− 50%

  • The results of our experimental study on the ignition and combustion of anthracite modified with a waste car tires pyrolysis oil additive in an amount of 5−30 wt

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Summary

■ INTRODUCTION

Coal is one of the main fuels for power generation worldwide.[1]. Its consumption declines very slowly making it relevant for the upcoming decades. With an increase in the temperature of the heating medium up to 800 °C, the duration of flame combustion was increased It was in good agreement with the results of other authors for combustion of a coal−water slurry mixed with waste turbine oil additives.[27] The formation of a flame was associated with the intense evaporation of light hydrocarbons of the pyrolysis oil and the simultaneous release of volatile matter of anthracite. For samples A10 and A20, the unburnt fuel was not observed This trend could be associated with the development of the surface structure and porosity of fuel particles (Figure 4) due to the intense release of gas-phase products formed during thermal transformation of anthracite samples with the pyrolysis oil additive. The similar gas emission features were reported for mixtures of coal with water and waste turbine oil,[28,29] which indirectly proves correctness of the obtained results

■ CONCLUSIONS
■ ACKNOWLEDGMENTS
■ REFERENCES
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