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Thermal degradation of real-world waste plastics and simulated mixed plastics in a two-stage pyrolysis-catalysis reactor for fuel production

机译:在用于燃料生产的两级热解催化反应器中,现实世界废塑料和模拟混合塑料的热降解

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摘要

Real-world postconsumer mixed plastics and a simulated mixture of plastics were processed in a two-stage pyrolysis-catalysis fixed bed reactor in the presence of a zeolite HZSM-5 catalyst. In addition, single plastic polyethylene, polypropylene, polystyrene, and polyethylene terephthalate were also processed in the two-stage reactor. The product yield, composition, and hydrocarbon distribution of the product oil was obtained in relation to plastic type. Noncatalytic pyrolysis of the plastics produced a high yield of an oil/wax product in the 81-97 wt % range. Addition of the catalyst reduced the yield of oil to between 44 and 51 wt %, with an increase in gas yield from cracking of the oil volatiles. However, the condensed oils produced from pyrolysis-catalysis were enriched with lower molecular weight (C-C) hydrocarbons and were markedly more aromatic in composition with a high proportion of single-ring aromatic hydrocarbons. Comparison of the results from pyrolysis and pyrolysis-catalysis of the simulated mixture of plastics with the data obtained for the individual plastics showed that significant interaction between the plastics occurred in the mixture with higher C-C gas yield and higher aromatic content in the oils than expected from the proportions of the individual plastics in the mixture.
机译:在沸石HZSM-5催化剂的存在下,在两级热解催化固定床反应器中处理了现实世界中的消费后混合塑料和模拟塑料混合物。另外,还在两级反应器中加工了单一塑料聚乙烯,聚丙烯,聚苯乙烯和聚对苯二甲酸乙二酯。获得与塑料类型有关的产物油的产物收率,组成和烃分布。塑料的非催化热解在81-97 wt%的范围内产生了高产率的油/蜡产品。催化剂的添加将油的产率降低至44至51重量%,并且由于油挥发物裂化而产生的气体产率增加。但是,由热解催化生产的冷凝油富含低分子量(C-C)烃,并且在组成上具有较高比例的单环芳族烃,因此明显具有更多的芳族化合物。将模拟的塑料混合物的热解和热解催化结果与各个塑料获得的数据进行比较,结果表明,混合物中的塑料之间发生了显着的相互作用,其CC气体收率更高,油中的芳烃含量也高于预期。混合物中各个塑料的比例。

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