TY - JOUR
T1 - Boron-Modified Mesoporous ZSM-5 for the Conversion of Pyrolysis Vapors from LDPE and Mixed Polyolefins: Maximizing the C2–C4 Olefin Yield with Minimal Carbon Footprint
AU - Eschenbacher, Andreas
AU - Goodarzi, Farnoosh
AU - Varghese, Robin John
AU - Enemark-Rasmussen, Kasper
AU - Kegnæs, Søren
AU - Abbas-Abadi, Mehrdad Seifali
AU - Van Geem, Kevin Marcel
PY - 2021
Y1 - 2021
N2 - Recovering monomers from polyolefins is challenging due to their chemical inertness. Chemical recycling via pyrolysis produces a complexliquid requiring subsequent upgrading and further processing. In the presented work, low-density polyethylene and postconsumer mixed polyolefin (MPO) waste were pyrolyzed at 550 °C and the vapors were passedover a catalyst to maximize the production of monomers, that is, light olefins and aromatics, which could produce new polymers in a circular approach. Hierarchical HZSM-5 zeolites containing both micro- and mesopores and their boron-modified versions with medium and high Si/Al ratios were studied and thoroughly characterized. The effect of catalyst temperature (550–700 °C), catalyst/feed ratio, steam treatment, and catalyst deactivation by coking was investigated using a tandem micropyrolyzer coupled to comprehensive two-dimensional gas chromatography and flame ionization detection/time-of-flight mass spectrometry detectors, allowing a detailed identification and quantification of the products. All catalysts effectively narrowed the product distribution with high selectivity toward C2–C4 olefins, monoaromatics,and C5–C11 aliphatics. HZSM-5 zeolite catalysts with a medium Si/Al ratio showed a higher monomer recovery (∼90%) than high Si/Al (∼80%), which has a higher selectivity to C5–C11 aliphatics. Importantly, the product yield distribution from MPO closely resembled low-density polyethylene. The addition of boron to the zeolite reduced the aromatization activity. Similarly, at comparable conversion levels, mild steam treatment of the catalyst lowered the selectivity to aromatics and increasedthe recovery of C2–C4 olefins. Hierarchical HZSM-5 zeolite showed improved tolerance against deactivation by coking compared to conventional HZSM-5, demonstrating the potential of boron-modified hierarchical HZSM-5 zeolite to recover monomers from polyolefin waste at high selectivity. Catalytic upgrading of pyrolysis vapors derived from waste polyolefin over modified zeolite catalysts selectively produces basec hemicals, which can increase the circularity by producing new plastics from these waste-produced base chemicals.
AB - Recovering monomers from polyolefins is challenging due to their chemical inertness. Chemical recycling via pyrolysis produces a complexliquid requiring subsequent upgrading and further processing. In the presented work, low-density polyethylene and postconsumer mixed polyolefin (MPO) waste were pyrolyzed at 550 °C and the vapors were passedover a catalyst to maximize the production of monomers, that is, light olefins and aromatics, which could produce new polymers in a circular approach. Hierarchical HZSM-5 zeolites containing both micro- and mesopores and their boron-modified versions with medium and high Si/Al ratios were studied and thoroughly characterized. The effect of catalyst temperature (550–700 °C), catalyst/feed ratio, steam treatment, and catalyst deactivation by coking was investigated using a tandem micropyrolyzer coupled to comprehensive two-dimensional gas chromatography and flame ionization detection/time-of-flight mass spectrometry detectors, allowing a detailed identification and quantification of the products. All catalysts effectively narrowed the product distribution with high selectivity toward C2–C4 olefins, monoaromatics,and C5–C11 aliphatics. HZSM-5 zeolite catalysts with a medium Si/Al ratio showed a higher monomer recovery (∼90%) than high Si/Al (∼80%), which has a higher selectivity to C5–C11 aliphatics. Importantly, the product yield distribution from MPO closely resembled low-density polyethylene. The addition of boron to the zeolite reduced the aromatization activity. Similarly, at comparable conversion levels, mild steam treatment of the catalyst lowered the selectivity to aromatics and increasedthe recovery of C2–C4 olefins. Hierarchical HZSM-5 zeolite showed improved tolerance against deactivation by coking compared to conventional HZSM-5, demonstrating the potential of boron-modified hierarchical HZSM-5 zeolite to recover monomers from polyolefin waste at high selectivity. Catalytic upgrading of pyrolysis vapors derived from waste polyolefin over modified zeolite catalysts selectively produces basec hemicals, which can increase the circularity by producing new plastics from these waste-produced base chemicals.
KW - Catalytic fast pyrolysis
KW - Zeolite
KW - Chemical recycling
KW - Polyethylene
KW - BTX
KW - Propylene
U2 - 10.1021/acssuschemeng.1c06098
DO - 10.1021/acssuschemeng.1c06098
M3 - Journal article
SN - 2168-0485
VL - 9
SP - 14618
EP - 14630
JO - ACS Sustainable Chemistry and Engineering
JF - ACS Sustainable Chemistry and Engineering
IS - 43
ER -