Abstract

Excessive untreated waste tires (WT) have posed threats to the environment and human health. Pyrolysis-catalysis, as a promising treatment technology, could convert WT into high-valued products such as pyrolysis oil. Moreover, BTX compounds (Benzene, toluene, and xylene) were important raw materials in the chemical industry. In order to sharply increase the BTX selectivity in the pyrolytic oil, transition metals (Ni and Fe) were impregnated on the ZSM-5 catalyst. Furthermore, this paper also explored the effect of catalysis modes, catalysts-to-feedstock mass ratios, and catalysis temperatures on the distribution of the aromatics in the WT pyrolysis-catalysis oil. The results suggested that the optimal operating parameters for BTX compound production with a selectivity of 39.87% were in-situ mode, catalysis temperature=600 °C, and catalyst-to-feedstock mass ratio=1:1 by applying Ni/ZSM-5. According to the GC-MS identification results, it proposed that the Diels-Alder reaction of isoprene and cracking and recombination of limonene in the aliphatic hydrocarbon pool were the main paths to generate the aromatics, while the addition of ethylene radicals in the monocyclic aromatic hydrocarbon (MAH) and polycyclic aromatic hydrocarbon (PAH) pools was dominant in the growth of the aromatics. The study provided a viable approach for upgrading WT to produce high-value aromatic products.

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