TY - JOUR
T1 - Highly selective conversion of mixed polyolefins to valuable base chemicals using phosphorus-modified and steam-treated mesoporous HZSM-5 zeolite with minimal carbon footprint
AU - Eschenbacher, Andreas
AU - Varghese, Robin John
AU - Delikonstantis, Evangelos
AU - Mynko, Oleksii
AU - Goodarzi, Farnoosh
AU - Enemark-Rasmussen, Kasper
AU - Oenema, Jogchum
AU - Abbas-Abadi, Mehrdad Seifali
AU - Stefanidis, Georgios D.
AU - Van Geem, Kevin M.
PY - 2022
Y1 - 2022
N2 - Catalytic fast pyrolysis of polyolefinic waste streams was investigated to recover valuable base chemicals at high selectivity. HZSM-5 zeolite with different properties, affected by Si/Al, mesoporosity, phosphorus stabilization, and steaming, were tested and thoroughly characterized. Different feeds, catalyst/feed ratios and reaction temperatures were evaluated in a micropyrolysis reactor coupled to two-dimensional gas chromatography. While unmodified HZSM-5 rapidly deactivated, phosphorus-modified and steamtreated HZSM-5 showed almost no deactivation due to its lower coking propensity during 130 runs with stable conversion towards C5+ aliphatics and high C2-C4 olefins selectivity (~75%) using post-consumer mixed polyolefins. The performance of this direct olefins production route with unprecedented high olefin selectivity was further evaluated in a plantwide context. It was found that it requires ~37% lower energy input than the plastics pyrolysis followed by pyrolytic oil steam cracking, while it results to at least a one order of magnitude lower environmental burden as compared to waste incineration.
AB - Catalytic fast pyrolysis of polyolefinic waste streams was investigated to recover valuable base chemicals at high selectivity. HZSM-5 zeolite with different properties, affected by Si/Al, mesoporosity, phosphorus stabilization, and steaming, were tested and thoroughly characterized. Different feeds, catalyst/feed ratios and reaction temperatures were evaluated in a micropyrolysis reactor coupled to two-dimensional gas chromatography. While unmodified HZSM-5 rapidly deactivated, phosphorus-modified and steamtreated HZSM-5 showed almost no deactivation due to its lower coking propensity during 130 runs with stable conversion towards C5+ aliphatics and high C2-C4 olefins selectivity (~75%) using post-consumer mixed polyolefins. The performance of this direct olefins production route with unprecedented high olefin selectivity was further evaluated in a plantwide context. It was found that it requires ~37% lower energy input than the plastics pyrolysis followed by pyrolytic oil steam cracking, while it results to at least a one order of magnitude lower environmental burden as compared to waste incineration.
KW - Pyrolysis
KW - Catalyst
KW - CO2 footprint
KW - Chemical recycling
KW - Olefins
KW - Plastic waste
U2 - 10.1016/j.apcatb.2022.121251
DO - 10.1016/j.apcatb.2022.121251
M3 - Journal article
SN - 0926-3373
VL - 309
JO - Applied Catalysis B: Environmental
JF - Applied Catalysis B: Environmental
M1 - 121251
ER -