沸石
聚丙烯
催化作用
开裂
化学工程
材料科学
碳氢化合物
烷烃
有机化学
化学
工程类
作者
Yukio Ando,Takumi Miyakage,Alisa Phuekphong,Akihiko Anzai,Mengwen Huang,Abdellah Ait El Fakir,Takashi Toyao,Makoto Ogawa,Alexander A. Kolganov,Evgeny A. Pidko,Ken‐ichi Shimizu
标识
DOI:10.1002/cctc.202500512
摘要
Abstract Chemical recycling of polyolefins represented by polyethylene (PE) and polypropylene (PP) via catalytic cracking has emerged as a promising strategy for converting waste plastics into valuable hydrocarbons. In this study, we investigated the selective hydrocracking of PP into light alkanes (C 1 –C 5 ) using zeolite catalysts at 280 °C under 1 MPa H 2 . An HMFI zeolite with high Al content exhibited the best catalytic performance among various zeolite catalysts tested. In situ DRIFTS comparing bare HMFI and externally‐silylated HMFI suggested that the external surface Brønsted acid sites serve as the active sites for the cracking of PP. Combination of in situ DRIFTS and UV–vis spectroscopy analyses identified the formation and consumption of oligomeric species as a reaction intermediate during reaction. Density functional theory (DFT) calculations suggested that a route in which the carbocation and alkoxide intermediates generated by hydrocracking of PP undergo low‐energy barrier transformations into gaseous products such as C 3 and C 4 hydrocarbons. This study advances the development of sustainable polyolefin recycling technologies.
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