Understanding of synergy in non-isothermal microwave-assisted in-situ catalytic co-pyrolysis of rice husk and polystyrene waste mixtures
| dc.contributor.author | Sridevi, V. | |
| dc.contributor.author | Suriapparao, D.V. | |
| dc.contributor.author | Tukarambai, M. | |
| dc.contributor.author | Terapalli, A. | |
| dc.contributor.author | Ramesh, R. | |
| dc.contributor.author | Sankar Rao, C.S. | |
| dc.contributor.author | Gautam, R. | |
| dc.contributor.author | Moorthy, J.V. | |
| dc.contributor.author | Suresh Kumar, C. | |
| dc.date.accessioned | 2026-02-04T12:27:44Z | |
| dc.date.issued | 2022 | |
| dc.description.abstract | Rice husk (RH) and polystyrene (PS) wastes were converted into value-added products using microwave-assisted catalytic co-pyrolysis. The graphite susceptor (10 g) along with KOH catalyst (5 g) was mixed with the feedstock to understand the products and energy consumption. RH promoted the char yield (20–34 wt%) and gaseous yields (16–25 wt%) whereas PS enhanced the oil yield (23–70 wt%). Co-pyrolysis synergy induced an increase in gaseous yields (14–53 wt%) due to excessive cracking. The specific microwave energy consumption dramatically decreased in co-pyrolysis (5–22 kJ/g) compared to pyrolysis (56–102 kJ/g). The pyrolysis index increased (17–445) with the increase in feedstock quantity (5–50 g). The obtained oil was composed of monoaromatics (74%) and polyaromatics (18%). The char was rich in carbon content (79.5 wt%) and the gases were composed of CO (24%), H<inf>2</inf> (12%), and CH<inf>4</inf> (22%). © 2022 Elsevier Ltd | |
| dc.identifier.citation | Bioresource Technology, 2022, 360, , pp. - | |
| dc.identifier.issn | 9608524 | |
| dc.identifier.uri | https://doi.org/10.1016/j.biortech.2022.127589 | |
| dc.identifier.uri | https://idr.nitk.ac.in/handle/123456789/22429 | |
| dc.publisher | Elsevier Ltd | |
| dc.subject | Energy utilization | |
| dc.subject | Feedstocks | |
| dc.subject | Microwaves | |
| dc.subject | Potassium hydroxide | |
| dc.subject | Pyrolysis | |
| dc.subject | Copyrolysis | |
| dc.subject | Energy-consumption | |
| dc.subject | Microwave-assisted | |
| dc.subject | Nonisothermal | |
| dc.subject | Polystyrene waste | |
| dc.subject | Rice husk | |
| dc.subject | Susceptors | |
| dc.subject | Synergistic effect | |
| dc.subject | Value added products | |
| dc.subject | Waste mixtures | |
| dc.subject | Polystyrenes | |
| dc.subject | aliphatic hydrocarbon | |
| dc.subject | aromatic compound | |
| dc.subject | biogas | |
| dc.subject | carbon | |
| dc.subject | charcoal | |
| dc.subject | cycloalkane | |
| dc.subject | cycloalkene | |
| dc.subject | polystyrene | |
| dc.subject | zeolite | |
| dc.subject | polystyrene derivative | |
| dc.subject | catalyst | |
| dc.subject | Article | |
| dc.subject | catalysis | |
| dc.subject | chemical composition | |
| dc.subject | controlled study | |
| dc.subject | cross validation | |
| dc.subject | energy consumption | |
| dc.subject | environmental temperature | |
| dc.subject | gas | |
| dc.subject | heating | |
| dc.subject | k fold cross validation | |
| dc.subject | machine learning | |
| dc.subject | mass fragmentography | |
| dc.subject | microwave radiation | |
| dc.subject | pyrolysis | |
| dc.subject | rice husk | |
| dc.subject | support vector machine | |
| dc.subject | valorization | |
| dc.subject | waste | |
| dc.subject | heat | |
| dc.subject | Oryza | |
| dc.subject | Catalysis | |
| dc.subject | Gases | |
| dc.subject | Hot Temperature | |
| dc.title | Understanding of synergy in non-isothermal microwave-assisted in-situ catalytic co-pyrolysis of rice husk and polystyrene waste mixtures |
