Oil produced from Ghana cocoa bean for potential industrial applications

被引:0
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作者
Tulashie, Samuel Kofi [1 ]
Dodoo, Daniel [2 ,3 ]
Appiah, Godfred [4 ,5 ]
Kotoka, Francis [5 ]
Adukpoh, Kingsley Enoch [6 ]
机构
[1] Industrial Chemistry Section, Department of Chemistry, School of Physical Sciences, College of Agriculture and Natural Sciences, University of Cape Coast, Takoradi - Cape Coast Rd, Cape Coast, Central Region P.M.B. University Post Office, Ghana
[2] Chemical Nanoengineering Section, Department of Industrial Engineering, School of Engineering, University of Rome Tor Vergata, Via Cracow 50, Rome,00133, Italy
[3] Department of Chemistry, Faculty of Science, Aix-Marseille University, 52 Avenue Escadrille Normandie Niemen, Marseille,Aix-en-Provence,13013, France
[4] Department of Water Supply, Sanitation and Environmental Engineering, IHE Delft Institute of Water Education, Westvest 7, Delft,2611AX, Netherlands
[5] Department of Green Chemistry and Technology, Faculty of Bioscience Engineering, Ghent University, Coupure Links 653, Gent,9000, Belgium
[6] Department of Chemistry, College of Science, Kwame Nkrumah University of Science and Technology, Kumasi,Ashanti Region, Ghana
关键词
Kinetics - Free energy - Mass transfer - Activation energy - Entropy;
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摘要
Cocoa bean (Theobroma cacao L.) oil is a promising intermediate cocoa product with few research demonstrating its potential for the direct production of industrial cocoa products. This study highlights the extraction and characterisations of oil obtained from the Ghana cocoa bean crop to evaluate its suitability for industrial applications. A solvent extraction method was employed to extract the oil at variable extraction temperatures and times. Kinetic and thermodynamic models were adopted to study the oil's extraction at varying temperatures and times. The maximum yield of the oil (21.62%) was reached at the highest temperature, 333 K (at 130 min), following first-order kinetics. The mass transfer (km) and regression coefficient (r2) were 0.0389 ± 0.0045 min−1 and 0.9993 ± 0.0005, respectively. The activation energy (Ea), entropy change (ΔS), equilibrium constant (K), and enthalpy change (ΔH) were 15.57 kJ mol−1, 276.13 J/(mol K)−1, 5.64, and 78.11 kJ mol−1, respectively. The activation enthalpy (ΔH*), entropy (ΔS*), and Gibb's free energy (ΔG*) were 12.87 ± 0.05 kJ mol−1, − 258.88 ± 0.17 J/(mol K)−1 and 97.13 ± 1.67 kJ mol−1, respectively, favouring a forward, irreversible, endothermic, and spontaneous extraction. The major fatty acids identified in the oil were stearic acid (37%), oleic acid (34%), and palmitic acid (26%). The iodine value, peroxide value, saponification value, unsaponification value, and free fatty acids of the oil were below the recommended standards acceptable for industrial applications. Differential scanning calorimetry–thermal gravimetric studies showed that the oil was thermally stable at high temperatures until thermal decomposition occurred around 260 °C. The oil's oxidation was monitored with computational modelling and Fourier infrared red spectroscopy, which found the oil highly stable despite the thermal extraction. © 2021 Elsevier B.V.
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