Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0)
Unfortunately, the original article contains error in Sect. 3.3. Fuel Composition. The correct data have been provided below in this correction article. 3.3. Fuel composition The fatty acid composition of the produced biodiesel through the optimisation process is shown in Table 8. From the table, it...
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my.uniten.dspace-271322023-05-29T17:40:00Z Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0) Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. 55936470700 6603918185 57855679400 55962751500 57929684200 55310784800 56997615100 Unfortunately, the original article contains error in Sect. 3.3. Fuel Composition. The correct data have been provided below in this correction article. 3.3. Fuel composition The fatty acid composition of the produced biodiesel through the optimisation process is shown in Table 8. From the table, it can be seen that Australian canola oil is mostly composed of methyl oleate, with 42.47 wt% included in the composition. This is followed by 27.85 wt% and 16.65 wt% methyl linoleate and methyl linoleate, respectively. A similar FAC was observed by Issariyakul and Dalai (2010) with slight difference in methyl oleate and methyl linolenate percentages. The main component of their canola oil biodiesel is methyl oleate which contains 60.92 wt% of this component. Based on the composition, canola biodiesel contains a total of 12.89 wt% saturated FAME component, 42.61 wt% monounsaturated FAME and 44.5 wt% polyunsaturated FAME. Table 9 compares the properties of produced canola biodiesel and diesel. According to the table, canola oil biodiesel has a 21.5% higher cetane number but a 6% lower LHV than diesel fuel. � The Author(s) 2022. Article in Press 2023-05-29T09:39:59Z 2023-05-29T09:39:59Z 2022 Erratum 10.1007/s10668-022-02617-8 2-s2.0-85136511238 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85136511238&doi=10.1007%2fs10668-022-02617-8&partnerID=40&md5=aceed661909a6cefd5972190b5169f6b https://irepository.uniten.edu.my/handle/123456789/27132 All Open Access, Hybrid Gold Springer Science and Business Media B.V. Scopus |
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Unfortunately, the original article contains error in Sect. 3.3. Fuel Composition. The correct data have been provided below in this correction article. 3.3. Fuel composition The fatty acid composition of the produced biodiesel through the optimisation process is shown in Table 8. From the table, it can be seen that Australian canola oil is mostly composed of methyl oleate, with 42.47 wt% included in the composition. This is followed by 27.85 wt% and 16.65 wt% methyl linoleate and methyl linoleate, respectively. A similar FAC was observed by Issariyakul and Dalai (2010) with slight difference in methyl oleate and methyl linolenate percentages. The main component of their canola oil biodiesel is methyl oleate which contains 60.92 wt% of this component. Based on the composition, canola biodiesel contains a total of 12.89 wt% saturated FAME component, 42.61 wt% monounsaturated FAME and 44.5 wt% polyunsaturated FAME. Table 9 compares the properties of produced canola biodiesel and diesel. According to the table, canola oil biodiesel has a 21.5% higher cetane number but a 6% lower LHV than diesel fuel. � The Author(s) 2022. |
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55936470700 Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. |
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Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. |
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Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0) |
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Hazrat M.A. |
title |
Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0) |
title_short |
Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0) |
title_full |
Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0) |
title_fullStr |
Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0) |
title_full_unstemmed |
Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2022), 10.1007/s10668-022-02506-0) |
title_sort |
correction: biodiesel production from transesterification of australian brassica napus l. oil: optimisation and reaction kinetic model development (environment, development and sustainability, (2022), 10.1007/s10668-022-02506-0) |
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Springer Science and Business Media B.V. |
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2023 |
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