The effect of torrefaction temperature and catalyst loading in Microwave-Assisted in-situ catalytic Co-Pyrolysis of torrefied biomass and plastic wastes
| dc.contributor.author | Ramesh, R. | |
| dc.contributor.author | Suriapparao, D.V. | |
| dc.contributor.author | Sankar Rao, C.S. | |
| dc.contributor.author | Sridevi, V. | |
| dc.contributor.author | Kumar, A. | |
| dc.contributor.author | Shah, M. | |
| dc.date.accessioned | 2026-02-04T12:27:32Z | |
| dc.date.issued | 2022 | |
| dc.description.abstract | In the current study, the effect of torrefaction temperatures (125–175 °C) and catalyst quantity (5–15 g) on co-pyrolysis of torrefied sawdust (TSD) and polystyrene (PS) are investigated to obtain value-added products. The role of torrefaction in co-pyrolysis of TSD: PS was analyzed to understand the product yields, synergy, and energy consumption. As the torrefaction temperature increases, oil yield (48.3–59.6 wt%) and char yield (24.3–29 wt%) increase while gas yield (27.4–11.4 wt%) decreases. Catalytic co-pyrolysis showed a significant level of synergy when compared to non-catalytic co-pyrolysis. For the conversion (%), a positive synergy maximum (-2.6) exists at a torrefaction temperature of 175 °C and 15 g of KOH catalyst. To develop the model, polynomial regression-based machine learning was used to predict pyrolysis product yields and energy usage variables. The developed models showed significant prediction accuracy (R2 > 0.98), suggesting the experimental values and the predicted values matched well. © 2022 Elsevier Ltd | |
| dc.identifier.citation | Bioresource Technology, 2022, 364, , pp. - | |
| dc.identifier.issn | 9608524 | |
| dc.identifier.uri | https://doi.org/10.1016/j.biortech.2022.128099 | |
| dc.identifier.uri | https://idr.nitk.ac.in/handle/123456789/22331 | |
| dc.publisher | Elsevier Ltd | |
| dc.subject | Catalysts | |
| dc.subject | Energy utilization | |
| dc.subject | Potassium hydroxide | |
| dc.subject | Pyrolysis | |
| dc.subject | Biomass wastes | |
| dc.subject | Catalyst loadings | |
| dc.subject | Copyrolysis | |
| dc.subject | Microwave-assisted | |
| dc.subject | Microwave-assisted pyrolysis | |
| dc.subject | Plastics waste | |
| dc.subject | Product yields | |
| dc.subject | Synergistic effect | |
| dc.subject | Temperature loadings | |
| dc.subject | Torrefaction | |
| dc.subject | Polystyrenes | |
| dc.subject | biogas | |
| dc.subject | polystyrene | |
| dc.subject | biomass | |
| dc.subject | catalyst | |
| dc.subject | machine learning | |
| dc.subject | pyrolysis | |
| dc.subject | Article | |
| dc.subject | energy consumption | |
| dc.subject | experimental design | |
| dc.subject | gas | |
| dc.subject | heating | |
| dc.subject | leave one out cross validation | |
| dc.subject | mathematical model | |
| dc.subject | microwave assisted catalytic co pyrolysis | |
| dc.subject | plastic waste | |
| dc.subject | predictive value | |
| dc.subject | sawdust | |
| dc.subject | temperature | |
| dc.subject | torrefied sawdust | |
| dc.title | The effect of torrefaction temperature and catalyst loading in Microwave-Assisted in-situ catalytic Co-Pyrolysis of torrefied biomass and plastic wastes |
