Abstract

The co-liquefaction of lignite coal and used tire was performed in a 250-ml batch reactor, in supercritical water under a nitrogen atmosphere to investigate the effects of temperature (380-440℃), water/feedstock ratio (4/1-10/1 (wt./wt.)) and the % used tire content in the feedstock (0-100 wt.%) on the conversion efficiency, liquid yield and oil composition attained. The maximum conversion and oil yield were 67 and 50%, respectively, obtained at 400℃ at 1 min, with water/feedstock ratio of 10/1 and 80% used tire content. The distillation characteristics of the oil products, analyzed by simulated distillation gas chromatography, revealed that the oil composition depended significantly on the reaction temperature. The co-liquefaction of coal and used tire yielded a synergistically increased level of oil production. Moreover, the total conversion level obtained with co-liquefaction alone was almost equal to those obtained in the presence of either Fe2O3 or NiMo as catalysts, under the same conditions. Therefore, supercritical water is a good medium for the dissolution of the volatile matter from a coal and used tire matrix.

Highlights

  • In recent years, the growth in tire consumption has continued to expand concomitantly leading to the problem of the disposal of an ever increasing number of essentially non-biodegredable but flammable spent scrap tires without causing environmental pollution

  • The co-liquefaction of lignite coal and used tire was performed in a 250-ml batch reactor, in supercritical water under a nitrogen atmosphere to investigate the effects of temperature (380-440°C), water/feedstock ratio (4/1-10/1) and the % used tire content in the feedstock (0-100 wt.%) on the conversion efficiency, liquid yield and oil composition attained

  • The total conversion and liquid yield obtained from the co-liquefaction of coal and waste tire attained were 66 and 50%, respectively, at the optimum reaction condition of 400°C for 1 min, with wa

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Summary

Introduction

The growth in tire consumption has continued to expand concomitantly leading to the problem of the disposal of an ever increasing number of essentially non-biodegredable but flammable spent scrap tires without causing environmental pollution (including combustion). Currently perhaps only 60-70% of all used tires are recycled, and evens this requires the use of environmentally and economically costly processes including the use of solvents like n-hexane, toluene and tetralin [2,3]. The well-developed techniques used in coal utilization should theoretically be applicable to the pyrolytic destruction of waste tires and there has been an increasing amount of attention paid to the co-utilization of coal and waste tires. Given that coal liquefaction is enhanced by the addition of crude oil [4] which is a source of rubber constituents in tires, the coliquefaction of coal and used tires is of obvious interest

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