热解
低密度聚乙烯
聚乙烯
聚烯烃
动力学
等温过程
产量(工程)
烧焦
化学工程
碳纤维
材料科学
化学动力学
化学
有机化学
热力学
复合材料
物理
工程类
复合数
量子力学
图层(电子)
作者
Isaac Mastalski,Nathan Sidhu,Ali Zolghadr,Saurabh Maduskar,Bryan Patel,Sundararajan Uppili,Tony Go,Ziwei Wang,Matthew Neurock,Paul J. Dauenhauer
标识
DOI:10.1021/acs.chemmater.3c00256
摘要
Continued demand for polyolefins can be met by recycling plastic materials back to their constituent monomers, ethylene and propylene, via thermal cracking in a pyrolysis reactor. During pyrolysis, saturated polyolefin chains break carbon–carbon and carbon–hydrogen bonds, yielding a distribution of alkanes, alkenes, aromatic chemicals, light gases, and solid char residues at temperatures varying from 400 to 800 °C. To design a pyrolysis reactor that optimizes the chemistry for a maximum yield of light olefins, a detailed description of the chemical mechanisms and associated kinetics is required. To that end, the reaction kinetics of isothermal films of low-density polyethylene (LDPE) have been measured by the method of “pulse-heated analysis of solid reactions”, or PHASR, which allows for quantification of intrinsic kinetics via isothermal reaction-controlled experimental conditions. The evolution of LDPE films from 20 ms to 2.0 s for five temperatures (550, 575, 600, 625, and 650 °C) was characterized by measurement of the yield of chromatography-detectable compounds (
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