TY - JOUR
T1 - Pyrolysis of mixed plastic waste (DKR-350)
T2 - Effect of washing pre-treatment and fate of chlorine
AU - Genuino, Homer C.
AU - Ruiz, M. Pilar
AU - Heeres, Hero J.
AU - Kersten, Sascha R. A.
N1 - Funding Information:
The authors gratefully acknowledge the Institute for Sustainable Process Technology (ISPT) of the Netherlands and the Dutch Polymer Institute (DPI) within the framework of the Circular Plastics Initiative Program (CP-50-02, Towards improved circularity of polyolefin-based packaging) and partners. The authors would also like to thank several additional partners involved in this work: Suster, B.V. for making the pyrolysis set-up available, Léon Rorhbach and Gert-Jan Boer from the University of Groningen for their technical assistance in products analyses, Maria Del Mar Barreiro and Marcel van Eijk from the Nationaal Testcentrum Circulare Plastics for sourcing the waste plastics used in this project, and Matthijs Ruitenbeek and Melissa Dunkle from Dow Benelux B.V. for providing analytical support for the analysis of waste plastics presented herein.
Funding Information:
The authors gratefully acknowledge the Institute for Sustainable Process Technology (ISPT) of the Netherlands and the Dutch Polymer Institute (DPI) within the framework of the Circular Plastics Initiative Program (CP-50-02, Towards improved circularity of polyolefin-based packaging) and partners. The authors would also like to thank several additional partners involved in this work: Suster, B.V. for making the pyrolysis set-up available, Léon Rorhbach and Gert-Jan Boer from the University of Groningen for their technical assistance in products analyses, Maria Del Mar Barreiro and Marcel van Eijk from the Nationaal Testcentrum Circulare Plastics for sourcing the waste plastics used in this project, and Matthijs Ruitenbeek and Melissa Dunkle from Dow Benelux B.V. for providing analytical support for the analysis of waste plastics presented herein.
Publisher Copyright:
© 2022
PY - 2022/8
Y1 - 2022/8
N2 - Pyrolysis of a post-consumer plastic waste stream (DKR-350) has been performed at a laboratory scale in a fixed-bed reactor at 500 °C. DKR-350 is a complex mixture of post-consumer plastics comprising polyethylene, polypropylene, polystyrene, polyethylene terephthalate, clogged materials, multilayer flexibles, together with considerable amounts of biogenic and inorganic residues and halogens. The influence of different washing procedures on feedstock composition and pyrolysis product yields was investigated. Washing effectively lowers the biogenic, inorganic and halogen contents in DKR-350, though does not affect the yield of the desired oil/wax (66 to 69 wt%). 27% of the oil/wax lies in the boiling point range of naphtha and gasoline (< 200 °C). During pyrolysis, the oxygen content of the oil/wax is reduced to 8–14 wt%, compared to 10–16 wt% in the feed. Chlorine analysis revealed that most of the chlorine present in the feed is removed by washing. Nevertheless, the concentration of chlorine in the oil/wax is still high (>150 ppm), showing the presence of recalcitrant organochlorides in the feed. Thus, post-treatment is still required to upgrade it to feedstock for the production of fuels and/or chemicals.
AB - Pyrolysis of a post-consumer plastic waste stream (DKR-350) has been performed at a laboratory scale in a fixed-bed reactor at 500 °C. DKR-350 is a complex mixture of post-consumer plastics comprising polyethylene, polypropylene, polystyrene, polyethylene terephthalate, clogged materials, multilayer flexibles, together with considerable amounts of biogenic and inorganic residues and halogens. The influence of different washing procedures on feedstock composition and pyrolysis product yields was investigated. Washing effectively lowers the biogenic, inorganic and halogen contents in DKR-350, though does not affect the yield of the desired oil/wax (66 to 69 wt%). 27% of the oil/wax lies in the boiling point range of naphtha and gasoline (< 200 °C). During pyrolysis, the oxygen content of the oil/wax is reduced to 8–14 wt%, compared to 10–16 wt% in the feed. Chlorine analysis revealed that most of the chlorine present in the feed is removed by washing. Nevertheless, the concentration of chlorine in the oil/wax is still high (>150 ppm), showing the presence of recalcitrant organochlorides in the feed. Thus, post-treatment is still required to upgrade it to feedstock for the production of fuels and/or chemicals.
KW - Chemical recycling
KW - Chlorine
KW - DKR-350
KW - Mixed plastic waste
KW - Pyrolysis
UR - http://www.scopus.com/inward/record.url?scp=85129731602&partnerID=8YFLogxK
U2 - 10.1016/j.fuproc.2022.107304
DO - 10.1016/j.fuproc.2022.107304
M3 - Article
AN - SCOPUS:85129731602
SN - 0378-3820
VL - 233
JO - Fuel processing technology
JF - Fuel processing technology
M1 - 107304
ER -