2022
DOI: 10.1016/j.wasman.2021.11.009
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Opportunities and challenges for the application of post-consumer plastic waste pyrolysis oils as steam cracker feedstocks: To decontaminate or not to decontaminate?

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Cited by 161 publications
(180 citation statements)
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References 282 publications
(420 reference statements)
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“…PT-Film sample registered the lowest chlorine content (160 ppm). This value, although low, is higher than the value established for use in existing petrochemical plants (3–10 ppm), as stated by some authors [ 51 , 52 , 53 ] However, these pyrolysis oils could probably be blended with other refinery streams before usage and most likely could be used as alternative fuels in cement kilns, where the required chlorine concentration is not usually so low. In the conditions of this work, about 10–30 wt.% of the chlorine content present in the waste samples was transferred to the liquid product.…”
Section: Resultsmentioning
confidence: 71%
“…PT-Film sample registered the lowest chlorine content (160 ppm). This value, although low, is higher than the value established for use in existing petrochemical plants (3–10 ppm), as stated by some authors [ 51 , 52 , 53 ] However, these pyrolysis oils could probably be blended with other refinery streams before usage and most likely could be used as alternative fuels in cement kilns, where the required chlorine concentration is not usually so low. In the conditions of this work, about 10–30 wt.% of the chlorine content present in the waste samples was transferred to the liquid product.…”
Section: Resultsmentioning
confidence: 71%
“…302 Untreated plastic waste pyrolysis oils with high levels of contaminants are not feasible feedstocks for steam cracking unless sufficiently diluted. 321 Contamination may lead to catalyst deactivation if catalytic upgrading of products is desired. For example, a municipal plastic waste pyrolysis plant in Idaho, U.S.A. produced an oil only suitable for low-value applications due to severe contamination.…”
Section: Variables Affecting Product Distributionmentioning
confidence: 99%
“…323,325 The combination of high heat and mass transfer rates are responsible for significant yields of light hydrocarbons and non-condensable gas from the pyrolysis of plastics in fluidized beds. 321,336 Disadvantages include comminution of plastics to achieve small feedstock particles, and complicated reactor setups. 291 Additionally, the high gas velocities required for fluidization can cause entrainment of char particles, requiring particulate separation downstream of the reactor.…”
Section: Reactor Configurationsmentioning
confidence: 99%
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“…310,312 The combination of high heat and mass transfer rates are responsible for significant yields of light hydrocarbons and noncondensable gas from the pyrolysis of plastics in fluidized beds. 304,323 Disadvantages include comminution of plastics to achieve small feedstock particles, and complicated reactor setups. 274 Additionally, the high gas velocities required for fluidization can cause entrainment of char particles, requiring particulate separation downstream of the reactor.…”
Section: Reactor Configurationsmentioning
confidence: 99%