Catalytic pyrolysis of HDPE in continuous mode over zeolite catalysts in a conical spouted bed reactor

By G. Elordi, M. Olazar, G. Lopez, M. Amutio, M. Artetxe, R. Aguado, J. Bilbao. 2009

242 citations recorded by the source corpus.

Subfields: Biomedical Engineering, Inorganic Chemistry, Polymers and Plastics

View Paper: https://www.semanticscholar.org/paper/3e98f6546f2b30544efbbb10b96b701ad512e831

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In Biomedical Engineering

1. J. Bilbao
2. M. Olazar
3. G. Lopez
4. M. Amutio
5. M. Artetxe
6. G. Elordi
7. Pankaj Kumar Tiwari
8. Pallabi Das

In Inorganic Chemistry

1. J. Bilbao
2. M. Olazar
3. G. Elordi
4. M. Amutio
5. M. Artetxe
6. G. Lopez

In Polymers and Plastics

1. J. Bilbao
2. M. Olazar
3. G. Lopez
4. M. Amutio
5. M. Artetxe
6. G. Elordi
7. Pankaj Kumar Tiwari
8. Pallabi Das

Citations in the corpus

• Light olefins from HDPE cracking in a two-step thermal and catalytic process (2012, background): “However, the HY zeolite is suitable for the production of C5–C11 hydrocarbons, but its deactivation is faster, and Hb zeolite performance is midway between HZSM-5 and HY [45,46].”
• Valorization of packaging plastic waste by slow pyrolysis (2018, methodology): “Various other reactor configurations like conical spouted bed reactor (Aguado et al., 2002c; Elordi et al., 2009), rotary kiln reactor (Aguado et al., 2002a; Serrano et al., 2003), microwave pyrolysis (Ludlow-Palafox and Chase, 2001b; Undri et al., 2013) etc. have also been utilized.”