Pyrolysis of high-density polyethylene in a fluidised bed reactor. Influence of the temperature and residence time
By F. J. Mastral, E. Esperanza, P. Garcı́a, M. Juste. 2002
275 citations recorded by the source corpus.
Subfields: Biomedical Engineering, Industrial and Manufacturing Engineering, Polymers and Plastics
View Paper: https://www.semanticscholar.org/paper/1c745ce3469a4bb047a7feb2bb8f1118e0b82346
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In Biomedical Engineering
In Industrial and Manufacturing Engineering
In Polymers and Plastics
Citations in the corpus
- Beyond Mechanical Recycling: Giving New Life to Plastic Waste (2020, unknown): “…residence times would T 5% T MAX PET ca. 0 [196] 400 [197] 435 [198] Benzoic acid, CO, CO 2 and solid organics [196] HDPE 40 (780 88 C, 1.3 s, –) [189] 415 [199][b] 460 [199] pyrolytic crude oil [200] PVC ca. 0 [201] 270 [202] 290 [202] , 465 [202][c] HCl, Benzene [201] LDPE 40 (860 88 C, 0.6 s,…”
- Kinetic study of high density polyethylene (HDPE) pyrolysis (2010, background): “However, the design and simulation of the reactors and the establishment of optimum process conditions requires an in-depth study of the thermal degradation of thermoplastic polymers to better understand the underlying parameters in general and pyrolysis kinetics specifically (Bilbao et al., 1997; M”