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Thermal pyrolysis of waste versus virgin polyolefin feedstocks: The role of pressure, temperature and waste composition

[Display omitted] •Pyrolysis of virgin and LDPE and PP wastes was performed in a pilot setup.•GC × GC was applied to identify and quantify the composition of the pyrolysis oils.•Identification of optimal temperature and pressure for pyrolysis.•The formation of preferentially propylene oligomers duri...

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Bibliographic Details
Published in:Waste management (Elmsford) 2023-06, Vol.165, p.108-118
Main Authors: Abbas-Abadi, Mehrdad Seifali, Kusenberg, Marvin, Zayoud, Azd, Roosen, Martijn, Vermeire, Florence, Madanikashani, Sepehr, Kuzmanović, Maja, Parvizi, Behzad, Kresovic, Uros, De Meester, Steven, Van Geem, Kevin M.
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Language:English
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Summary:[Display omitted] •Pyrolysis of virgin and LDPE and PP wastes was performed in a pilot setup.•GC × GC was applied to identify and quantify the composition of the pyrolysis oils.•Identification of optimal temperature and pressure for pyrolysis.•The formation of preferentially propylene oligomers during PP pyrolysis.•Plastic contaminations such as PVC and biomass intensify the coke formation. Due to the complexity and diversity of polyolefinic plastic waste streams and the inherent non-selective nature of the pyrolysis chemistry, the chemical decomposition of plastic waste is still not fully understood. Accurate data of feedstock and products that also consider impurities is, in this context, quite scarce. Therefore this work focuses on the thermochemical recycling via pyrolysis of different virgin and contaminated waste-derived polyolefin feedstocks (i.e., low-density polyethylene (LDPE), polypropylene (PP) as main components), along with an investigation of the decomposition mechanisms based on the detailed composition of the pyrolysis oils. Crucial in this work is the detailed chemical analysis of the resulting pyrolysis oils by comprehensive two-dimensional gas chromatography (GC × GC) and ICP-OES, among others. Different feedstocks were pyrolyzed at a temperature range of 430–490 °C and at pressures between 0.1 and 2 bar in a continuous pilot-scale pyrolysis unit. At the lowest pressure, the pyrolysis oil yield of the studied polyolefins reached up to 95 wt%. The pyrolysis oil consists of primarily α-olefins (37–42 %) and n-paraffins (32–35 %) for LDPE pyrolysis, while isoolefins (mostly C9 and C15) and diolefins accounted for 84–91 % of the PP-based pyrolysis oils. The post-consumer waste feedstocks led to significantly less pyrolysis oil yields and more char formation compared to their virgin equivalents. It was found that plastic aging, polyvinyl chloride (PVC) (3 wt%), and metal contamination were the main causes of char formation during the pyrolysis of polyolefin waste (4.9 wt%).
ISSN:0956-053X
1879-2456
DOI:10.1016/j.wasman.2023.04.029