Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method
This work investigates the optimization of reaction parameters with the Taguchi method for catalytic deoxygenation of waste cooking oil (WCO) as an alternative renewable fuel process. Commercial sulphated-ferric (II) oxide/alumina oxide catalyst has the potential as a deoxygenation catalyst due to i...
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my.uniten.dspace-342472024-10-14T11:18:37Z Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method Shafihi U. Hafriz R.S.R.M. Arifin N.A. Nor Shafizah I. Idris A. Salmiaton A. Razali N.M. 58111241700 57204588040 57195493347 57208543128 35576668200 57193906995 58111196100 Catalytic deoxygenation Green diesel Heterogeneous acid catalyst Optimization Pyrolysis Waste cooking oil Analysis of variance (ANOVA) Catalysts Diesel engines Hematite Physicochemical properties Taguchi methods Catalytic deoxygenation Deoxygenations Green diesels Heterogeneous acid catalysts N 2 flow Optimisations Pyrolysis oil Taguchi's methods Waste cooking oil ]+ catalyst Pyrolysis This work investigates the optimization of reaction parameters with the Taguchi method for catalytic deoxygenation of waste cooking oil (WCO) as an alternative renewable fuel process. Commercial sulphated-ferric (II) oxide/alumina oxide catalyst has the potential as a deoxygenation catalyst due to its good physicochemical properties which enhance the removal of oxygenated species. The obtained pyrolysis oil analysed by GC-MS revealed the selectivity of the pyrolysis oil mostly in the range of light diesel and kerosene fraction. From an analysis of variance (ANOVA), temperature awarded the most significant impact (86.62%) in this catalytic deoxygenation as compared to three other parameters followed by reaction time > N2 flow > catalyst loading. From the GC-MS analysis, the maximum renewable diesel fraction of 49.66% was obtained at 400 �C, 1 wt% of catalyst, 90 min of reaction time and 20 cm3/min N2 flow. The predicted model by Taguchi in the present study validated by the experimental work shows a promising application in optimising the catalytic pyrolysis process for future use. � 2023 The Authors Final 2024-10-14T03:18:37Z 2024-10-14T03:18:37Z 2023 Article 10.1016/j.rineng.2023.100959 2-s2.0-85148538334 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85148538334&doi=10.1016%2fj.rineng.2023.100959&partnerID=40&md5=7d61e89ed240efc0385878469934b8ab https://irepository.uniten.edu.my/handle/123456789/34247 17 100959 All Open Access Gold Open Access Elsevier B.V. Scopus |
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Catalytic deoxygenation Green diesel Heterogeneous acid catalyst Optimization Pyrolysis Waste cooking oil Analysis of variance (ANOVA) Catalysts Diesel engines Hematite Physicochemical properties Taguchi methods Catalytic deoxygenation Deoxygenations Green diesels Heterogeneous acid catalysts N 2 flow Optimisations Pyrolysis oil Taguchi's methods Waste cooking oil ]+ catalyst Pyrolysis |
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Catalytic deoxygenation Green diesel Heterogeneous acid catalyst Optimization Pyrolysis Waste cooking oil Analysis of variance (ANOVA) Catalysts Diesel engines Hematite Physicochemical properties Taguchi methods Catalytic deoxygenation Deoxygenations Green diesels Heterogeneous acid catalysts N 2 flow Optimisations Pyrolysis oil Taguchi's methods Waste cooking oil ]+ catalyst Pyrolysis Shafihi U. Hafriz R.S.R.M. Arifin N.A. Nor Shafizah I. Idris A. Salmiaton A. Razali N.M. Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method |
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This work investigates the optimization of reaction parameters with the Taguchi method for catalytic deoxygenation of waste cooking oil (WCO) as an alternative renewable fuel process. Commercial sulphated-ferric (II) oxide/alumina oxide catalyst has the potential as a deoxygenation catalyst due to its good physicochemical properties which enhance the removal of oxygenated species. The obtained pyrolysis oil analysed by GC-MS revealed the selectivity of the pyrolysis oil mostly in the range of light diesel and kerosene fraction. From an analysis of variance (ANOVA), temperature awarded the most significant impact (86.62%) in this catalytic deoxygenation as compared to three other parameters followed by reaction time > N2 flow > catalyst loading. From the GC-MS analysis, the maximum renewable diesel fraction of 49.66% was obtained at 400 �C, 1 wt% of catalyst, 90 min of reaction time and 20 cm3/min N2 flow. The predicted model by Taguchi in the present study validated by the experimental work shows a promising application in optimising the catalytic pyrolysis process for future use. � 2023 The Authors |
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58111241700 |
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58111241700 Shafihi U. Hafriz R.S.R.M. Arifin N.A. Nor Shafizah I. Idris A. Salmiaton A. Razali N.M. |
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Article |
author |
Shafihi U. Hafriz R.S.R.M. Arifin N.A. Nor Shafizah I. Idris A. Salmiaton A. Razali N.M. |
author_sort |
Shafihi U. |
title |
Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method |
title_short |
Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method |
title_full |
Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method |
title_fullStr |
Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method |
title_full_unstemmed |
Catalytic deoxygenation with SO42--Fe2O3/Al2O3 catalyst: Optimization by Taguchi method |
title_sort |
catalytic deoxygenation with so42--fe2o3/al2o3 catalyst: optimization by taguchi method |
publisher |
Elsevier B.V. |
publishDate |
2024 |
_version_ |
1814061173200388096 |
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13.214268 |