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Thermal and thermo-catalytic conversion of waste polyolefins to fuel-like mixture of hydrocarbons

机译:废聚烯烃的热催化和热催化转化为类燃料的烃混合物

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Results of the investigation of thermal degradation of polyolefins in the laboratory-scale set-upreactors are presented in the paper. Melting and cracking processes were carried out in two differenttypes of reactors at the temperature of 390-420°C. This article presents the results obtained forconversion of polyolefin waste in a reactor with a stirrer. Next, they were compared with the resultsobtained for the process carried out in a reactor with a molten metal bed, which was described in aprevious publication. For both processes, the final product consisted of a gaseous (2-16 % mass)and a liquid (84-98 % mass) part. No solid product was produced. The light, “gasoline” fraction ofthe liquid hydrocarbons mixture (C4-C10) made up over 50% of the liquid product. The overall(vapor) product may be used for electricity generation and the liquid product for fuel production.
机译:本文介绍了在实验室规模的装置反应器中对聚烯烃热降解的研究结果。在两种不同类型的反应器中,在390-420°C的温度下进行熔融和裂解过程。本文介绍了在带有搅拌器的反应器中转化聚烯烃废料获得的结果。接下来,将它们与在以前的出版物中描述的在具有熔融金属床的反应器中进行的方法获得的结果进行比较。对于这两个过程,最终产品均由气态(2-16%的质量)和液态(84-98%的质量)组成。没有产生固体产物。液态烃混合物(C4-C10)的轻质“汽油”馏分占液态产物的50%以上。整个(蒸气)产物可以用于发电,而液体产物可以用于燃料生产。

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