An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel Production

Plastic wastes are necessary to recycle due to their disposal issues around the world. They can be recycled through various techniques i.e., mechanical reprocessing, mechanical recycling, chemical recycling and incineration. Most recycling techniques are expensive and end up in producing low-grade p...

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Main Authors: Selvaganapathy Thambiyapillai, Muthuvelayudham Ramanujam
Format: Article
Language:English
Published: Diponegoro University 2021-11-01
Series:International Journal of Renewable Energy Development
Subjects:
Online Access:https://ijred.cbiore.id/index.php/ijred/article/view/33817
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author Selvaganapathy Thambiyapillai
Muthuvelayudham Ramanujam
author_facet Selvaganapathy Thambiyapillai
Muthuvelayudham Ramanujam
author_sort Selvaganapathy Thambiyapillai
collection DOAJ
description Plastic wastes are necessary to recycle due to their disposal issues around the world. They can be recycled through various techniques i.e., mechanical reprocessing, mechanical recycling, chemical recycling and incineration. Most recycling techniques are expensive and end up in producing low-grade products excluding chemical recycling; it is an eco-friendly way to deal with plastic waste. Catalytic cracking is one of the chemical recycling methods, for converting waste plastics into liquid fuel same as commercial fuels. An experimental investigation of polystyrene catalytic cracking process was conducted with impregnated fly ash catalyst and 88.4% of liquid product yield was found as a maximum at optimum operating conditions 425 ̊C and 60 min. The liquid fuel quality was analyzed using FTIR spectra analysis, GC/MS analysis and Physico-chemical property analysis. The GC/MS analysis shows that the fly ash cracking of polystyrene leads to the production of gasoline fuels within the hydrocarbon range of C3-C24, and the aliphatic and aromatic functional compounds were detected using FTIR analysis. Moreover, the Aspen Hysys simulation of polystyrene catalytic cracking was conducted in a pyrolytic reactor at 425 ̊C and at the end of the simulation, 93.6% of liquid fuel yield was predicted. It was inferred that the simulation model for the catalytic cracking is substantial to fit the experimental data in terms of liquid fuel conversion
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spelling doaj.art-90d34ee65c6d4de885b2cc1a715d81982023-11-28T02:08:36ZengDiponegoro UniversityInternational Journal of Renewable Energy Development2252-49402021-11-0110489190010.14710/ijred.2021.3381718900An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel ProductionSelvaganapathy Thambiyapillai0Muthuvelayudham Ramanujam1Tamilnadu Pollution Control Board (TNPCB), Tamilnadu, IndiaDepartment. of Chemical Engineering, Annamalai University, Chidambaram, Tamilnadu, IndiaPlastic wastes are necessary to recycle due to their disposal issues around the world. They can be recycled through various techniques i.e., mechanical reprocessing, mechanical recycling, chemical recycling and incineration. Most recycling techniques are expensive and end up in producing low-grade products excluding chemical recycling; it is an eco-friendly way to deal with plastic waste. Catalytic cracking is one of the chemical recycling methods, for converting waste plastics into liquid fuel same as commercial fuels. An experimental investigation of polystyrene catalytic cracking process was conducted with impregnated fly ash catalyst and 88.4% of liquid product yield was found as a maximum at optimum operating conditions 425 ̊C and 60 min. The liquid fuel quality was analyzed using FTIR spectra analysis, GC/MS analysis and Physico-chemical property analysis. The GC/MS analysis shows that the fly ash cracking of polystyrene leads to the production of gasoline fuels within the hydrocarbon range of C3-C24, and the aliphatic and aromatic functional compounds were detected using FTIR analysis. Moreover, the Aspen Hysys simulation of polystyrene catalytic cracking was conducted in a pyrolytic reactor at 425 ̊C and at the end of the simulation, 93.6% of liquid fuel yield was predicted. It was inferred that the simulation model for the catalytic cracking is substantial to fit the experimental data in terms of liquid fuel conversionhttps://ijred.cbiore.id/index.php/ijred/article/view/33817catalytic crackingpolystyreneaspen hysys simulationfly ashgasoline fuelsftir perkin elmer analyzer. .
spellingShingle Selvaganapathy Thambiyapillai
Muthuvelayudham Ramanujam
An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel Production
International Journal of Renewable Energy Development
catalytic cracking
polystyrene
aspen hysys simulation
fly ash
gasoline fuels
ftir perkin elmer analyzer. .
title An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel Production
title_full An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel Production
title_fullStr An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel Production
title_full_unstemmed An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel Production
title_short An Experimental Investigation and Aspen HYSYS Simulation of Waste Polystyrene Catalytic Cracking Process for the Gasoline Fuel Production
title_sort experimental investigation and aspen hysys simulation of waste polystyrene catalytic cracking process for the gasoline fuel production
topic catalytic cracking
polystyrene
aspen hysys simulation
fly ash
gasoline fuels
ftir perkin elmer analyzer. .
url https://ijred.cbiore.id/index.php/ijred/article/view/33817
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