Abstract

The ubiquitous challenges caused by the accumulation of mismanaged plastic solid wastes have seriously endangered ecological health. For enhancing the sustainable and environment-friendly conversion of mixed plastic packaging wastes into high-value benzene, toluene, ethylbenzene, and xylene (BTEX) while effectively reducing the coke deposition on catalysts, tandem catalytic pyrolysis of mixed packaging plastics over dual catalysts (MCM-41 and HZSM-5) was explored via a combination of in-situ catalysis and ex-situ catalysis in a two-stage fixed bed reactor. The selectivity of total and monocyclic aromatic hydrocarbons was nearly 100% and 85% with MCM-41 (500 °C) followed by HZSM-5 (550 °C), respectively. The BTEX production (245.33 mg/g) was considerably improved as compared to ex-situ catalysis of HZSM-5 (185.30 mg/g) and MCM-41/HZSM-5 (209.14 mg/g). Moreover, the total coke amount of tandem catalysis decreased to 14.25 mg/g than that of ex-situ catalysis of HZSM-5 (30.72 mg/g). The mechanisms analysis revealed that the pre-reforming effect of MCM-41 suppressed polycyclic aromatic hydrocarbons (PAHs) formation and coke deposition on the following HZSM-5 and meanwhile improved the utilization of internal acid sites for obtaining high-yield BTEX.

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