Production of valuable chemicals via multiphase catalytic pyrolysis of hazardous waste expanded polystyrene using low cost CaCO3 solid base catalyst
| dc.contributor.author | Verma A.; Pramanik H. | |
| dc.date.accessioned | 2025-05-23T11:13:06Z | |
| dc.description.abstract | In the present research work, multiphase catalytic pyrolysis (in-situ catalytic cracking) of waste expanded polystyrene (WEPS) has been carried out using calcium carbonate (CaCO3) as a solid base catalyst. The multiphase catalytic pyrolysis of WEPS has been conducted at different temperatures ranging from 400oC to 700oC at a heating rate of 15oC/min and feed to catalyst ratio of 20:1. The thermal pyrolysis of WEPS has produced a maximum liquid yield of 94.37 wt.% at a reaction temperature of 650oC and heating rate of 15oC/min. Whereas, the maximum liquid yield of 85.99 wt.% is obtained at a reaction temperature of 550oC and heating rate of 15oC/min for the multiphase catalytic pyrolysis. The GC-FID analysis confirm that the thermal pyrolysis oil is mainly composed of benzene (0.62 wt.%), toluene (10.21 wt.%), ethylbenzene (0.55 wt.%) and styrene (84.74 wt.%). Whereas, the pyrolysis oil obtained from multiphase catalytic pyrolysis using CaCO3 catalyst contains very high styrene content of 93.24 wt.% along with a very low amount of fuel range hydrocarbons benzene (0.25 wt.%), toluene (2.09 wt.%) and ethyl benzene (0.52 wt.%). Thus, the present study clearly indicates that the basic catalyst CaCO3 shows the high selectivity towards the styrene monomer. © 2024, National Institute of Science Communication and Policy Research. All rights reserved. | |
| dc.identifier.doi | https://doi.org/10.56042/ijct.v31i1.7610 | |
| dc.identifier.uri | http://172.23.0.11:4000/handle/123456789/5465 | |
| dc.relation.ispartofseries | Indian Journal of Chemical Technology | |
| dc.title | Production of valuable chemicals via multiphase catalytic pyrolysis of hazardous waste expanded polystyrene using low cost CaCO3 solid base catalyst |