LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP

Supercritical fluid extraction (SFE) is a green processing technique that employed the use of carbon dioxide (CO2) as an extractant in place of organic or inorganic solvents. In this study, SFE was used to recover oil from the milled palm fruit peels as a sustainable feedstock. The process was carri...

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Published in:Journal of Oil Palm Research
Main Author: Bello U.; Amran N.A.; Samsuri S.; Ruslan M.S.H.
Format: Article
Language:English
Published: Lembaga Minyak Sawit Malaysia 2023
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85160571720&doi=10.21894%2fjopr.2023.0020&partnerID=40&md5=560b9273cb56d49568b88a7b53c0ff53
id 2-s2.0-85160571720
spelling 2-s2.0-85160571720
Bello U.; Amran N.A.; Samsuri S.; Ruslan M.S.H.
LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
2023
Journal of Oil Palm Research
35
4
10.21894/jopr.2023.0020
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85160571720&doi=10.21894%2fjopr.2023.0020&partnerID=40&md5=560b9273cb56d49568b88a7b53c0ff53
Supercritical fluid extraction (SFE) is a green processing technique that employed the use of carbon dioxide (CO2) as an extractant in place of organic or inorganic solvents. In this study, SFE was used to recover oil from the milled palm fruit peels as a sustainable feedstock. The process was carried out at five different temperatures of 40°C-80°C, varied extraction time of 30-150 min, a fixed pressure of 25 MPa, a flow rate of 5 mL min–1, and a co-solvent ratio of 5.00% vol. The result shows that an optimum extract yield of 3.95% was recovered at the maximum temperature (80°C) after 150 min. The experimentally obtained data were subjected to kinetic analysis using Elovich’s, Hyperbolic and Pseudo second-order models. Models’ suitability to the data fitness was tested using seven error functions, in which Elovich’s was found to be the best-fitted model, succeeded by the Hyperbolic and then Pseudo second-order. Also, the result of statistical analysis using ANOVA, indicates that temperature has more impact on improving the rate of extract recovery than extraction time. Finally, the thermodynamic studies revealed that an irreversible and endothermically forward reaction was observed considering the values of the entropy change (ΔS) = 0.138 J mol–1 K–1, enthalpy change (ΔH) = 53.50 K J mol–1, and Gibbs’ free energy, (ΔG) = -6.04 K J mol–1 respectively. © 2023 Lembaga Minyak Sawit Malaysia. All rights reserved.
Lembaga Minyak Sawit Malaysia
15112780
English
Article
All Open Access; Gold Open Access
author Bello U.; Amran N.A.; Samsuri S.; Ruslan M.S.H.
spellingShingle Bello U.; Amran N.A.; Samsuri S.; Ruslan M.S.H.
LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
author_facet Bello U.; Amran N.A.; Samsuri S.; Ruslan M.S.H.
author_sort Bello U.; Amran N.A.; Samsuri S.; Ruslan M.S.H.
title LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
title_short LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
title_full LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
title_fullStr LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
title_full_unstemmed LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
title_sort LINEAR KINETICS MODELLING AND THERMODYNAMICS STUDY OF SUPERCRITICAL CO2-DERIVED OIL EXTRACTS FROM PALM FRUIT MESOCARP
publishDate 2023
container_title Journal of Oil Palm Research
container_volume 35
container_issue 4
doi_str_mv 10.21894/jopr.2023.0020
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85160571720&doi=10.21894%2fjopr.2023.0020&partnerID=40&md5=560b9273cb56d49568b88a7b53c0ff53
description Supercritical fluid extraction (SFE) is a green processing technique that employed the use of carbon dioxide (CO2) as an extractant in place of organic or inorganic solvents. In this study, SFE was used to recover oil from the milled palm fruit peels as a sustainable feedstock. The process was carried out at five different temperatures of 40°C-80°C, varied extraction time of 30-150 min, a fixed pressure of 25 MPa, a flow rate of 5 mL min–1, and a co-solvent ratio of 5.00% vol. The result shows that an optimum extract yield of 3.95% was recovered at the maximum temperature (80°C) after 150 min. The experimentally obtained data were subjected to kinetic analysis using Elovich’s, Hyperbolic and Pseudo second-order models. Models’ suitability to the data fitness was tested using seven error functions, in which Elovich’s was found to be the best-fitted model, succeeded by the Hyperbolic and then Pseudo second-order. Also, the result of statistical analysis using ANOVA, indicates that temperature has more impact on improving the rate of extract recovery than extraction time. Finally, the thermodynamic studies revealed that an irreversible and endothermically forward reaction was observed considering the values of the entropy change (ΔS) = 0.138 J mol–1 K–1, enthalpy change (ΔH) = 53.50 K J mol–1, and Gibbs’ free energy, (ΔG) = -6.04 K J mol–1 respectively. © 2023 Lembaga Minyak Sawit Malaysia. All rights reserved.
publisher Lembaga Minyak Sawit Malaysia
issn 15112780
language English
format Article
accesstype All Open Access; Gold Open Access
record_format scopus
collection Scopus
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