Evaluation of the applicability of polymeric materials to BTEX and fine product transformation by catalytic and non-catalytic pyrolysis as a part of the closed loop material economy

摘要

This article presents experimental results on the pyrolysis of different mixtures of polymer waste. ABS copolymer, PET, PP, tire waste styrene-butadiene rubber (SBR) and pure non-vulcanised SBR were used in the experiments under different catalyst conditions: (i) without a catalyst, (ii) with an unmodified ZSM-5 catalyst, (iii) with a ZSM-5 catalyst possessing ammonium groups, and (iv) with a ZSM-5 catalyst containing 10 % Ni. The primary objective of this study was to select suitable conditions to pyrolyse polymeric materials depending on the polymer type and properties of the desired final products, e.g., aromatic and heteroaromatic hydrocarbons and valuable chemical subproducts.Suitable conditions can be determined for the thermal conversion of polymeric materials, and using non catalytic pyrolysis can yield chemical compounds such as alpha-methyl styrene from acrylonitrile-butadienestyrene (ABS) and limonene from tire waste, which can be used in both fine chemicals and industrial production. The pyrolysis conditions can be modified in terms of the catalyst based on the tested waste polymer and result in products rich in BTEX fractions.Among all tested catalysts, the ZSM-5 catalyst based on aluminosilicate impregnated with nickel ions yielded the highest total fraction of aromatic and heteroaromatic hydrocarbons, especially from the pyrolysis of PP and PET. With this catalyst, more than 75 area% of the product stream (of the total identified product peaks by MS) consisted of aromatic and heteroaromatic fractions (e.g., terephthalonitrile from polyethylene terephthalate), which were composed of 5.6 and 19.9 area% benzene, 7.0 and 10.8 area% toluene, 5.7 and 10.6 area% ethyl benzene and 1.2 and 1.4 area% xylene for PP and PET, respectively. High proportions of the aromatic and heteroaromatic fractions were observed in the product stream during the ABS pyrolysis with two types of catalysts: aluminosilicate with ammonium groups (73 area% of the aromatic and heteroaromatic hydrocarbons) and aluminosilicate impregnated with nickel ions (85 area% of the aromatic and heteroaromatic hydrocarbons).