Staff View: Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2023), 25, 11, (12247-12272), 10.1007/s10668-022-02506-0)

Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2023), 25, 11, (12247-12272), 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. 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 Aust...

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Main Authors:	Hazrat M.A., Rasul M.G., Khan M.M.K., Ashwath N., Fattah I.M.R., Ong H.C., Mahlia T.M.I.
Other Authors:	55936470700
Format:	Erratum
Published:	Springer Science and Business Media B.V. 2025
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spelling	my.uniten.dspace-372002025-03-03T15:48:35Z Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2023), 25, 11, (12247-12272), 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 59273521300 55962751500 58776756000 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. 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. (Table presented.) Fatty acid composition of the produced canola biodiesel FAME group Linear structure Canola biodiesel (wt%) Canola oil (wt%) (Issariyakul and Dalai 2010) C8:0 CH3(CH2)6COOCH3 (Methyl caprylate) 0.19 ?C10:0 CH3(CH2)8 COOCH3 (Methyl caprate) 0.1 ?C12:0 CH3(CH2)10COOCH3 (Methyl laurate) 0.1 ?C14:0 CH3(CH2)12COOCH3 (Methyl myristate) 0.1 ?C16:0 CH3(CH2)14COOCH3 (Methyl palmitate) 6.35 4.36 C16:1 CH3(CH2)5CH=CH(CH2)7COOCH3 (Methyl palmitoleate) ?0.16 C18:0 CH3(CH2)16COOCH3 (Methyl stearate) 5.65 1.96 C18:1 CH3(CH2)7CH=CH(CH2)7COOCH3 (Methyl oleate) 42.47 60.92 C18:1(OH) CH3(CH2)5CH(OH)CH2CH=CH(CH2)7COOCH3 (Methyl ricinoleate) ?2.89 C18:2 CH3(CH2)4CH=CHCH2CH=CH(CH2)7COOCH3 (Methyl linoleate) 16.65 18.70 C18:3 CH3CH2CH=CHCH2CH=CHCH2CH=CH(CH2)7COOCH3 (Methyl linolenate) 27.85 6.79 C20:0 CH3(CH2)18COOCH3 (Methyl arachidate/Arachidic acid) 0.2 0.59 C22:0 CH3(CH2)20COO CH3 (Methyl behenate/hydroflo acid) 0.2 ?C22:1 CH3(CH2)7CH=CH(CH2)11COOCH3 (Methyl erucate/Heneicosanoic acid) 0.14 ?. ? 2022, The Author(s). Final 2025-03-03T07:48:35Z 2025-03-03T07:48:35Z 2024 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/123456789/37200 26 1 2739 2741 All Open Access; Hybrid Gold Open Access Springer Science and Business Media B.V. Scopus
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description	Unfortunately, the original article contains error in Sect.�3.3. Fuel Composition. The correct data have been provided below in this correction article. 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. (Table presented.) Fatty acid composition of the produced canola biodiesel FAME group Linear structure Canola biodiesel (wt%) Canola oil (wt%) (Issariyakul and Dalai 2010) C8:0 CH3(CH2)6COOCH3 (Methyl caprylate) 0.19 ?C10:0 CH3(CH2)8 COOCH3 (Methyl caprate) 0.1 ?C12:0 CH3(CH2)10COOCH3 (Methyl laurate) 0.1 ?C14:0 CH3(CH2)12COOCH3 (Methyl myristate) 0.1 ?C16:0 CH3(CH2)14COOCH3 (Methyl palmitate) 6.35 4.36 C16:1 CH3(CH2)5CH=CH(CH2)7COOCH3 (Methyl palmitoleate) ?0.16 C18:0 CH3(CH2)16COOCH3 (Methyl stearate) 5.65 1.96 C18:1 CH3(CH2)7CH=CH(CH2)7COOCH3 (Methyl oleate) 42.47 60.92 C18:1(OH) CH3(CH2)5CH(OH)CH2CH=CH(CH2)7COOCH3 (Methyl ricinoleate) ?2.89 C18:2 CH3(CH2)4CH=CHCH2CH=CH(CH2)7COOCH3 (Methyl linoleate) 16.65 18.70 C18:3 CH3CH2CH=CHCH2CH=CHCH2CH=CH(CH2)7COOCH3 (Methyl linolenate) 27.85 6.79 C20:0 CH3(CH2)18COOCH3 (Methyl arachidate/Arachidic acid) 0.2 0.59 C22:0 CH3(CH2)20COO CH3 (Methyl behenate/hydroflo acid) 0.2 ?C22:1 CH3(CH2)7CH=CH(CH2)11COOCH3 (Methyl erucate/Heneicosanoic acid) 0.14 ?. ? 2022, The Author(s).
author2	55936470700
author_facet	55936470700 Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I.
format	Erratum
author	Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I.
spellingShingle	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, (2023), 25, 11, (12247-12272), 10.1007/s10668-022-02506-0)
author_sort	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, (2023), 25, 11, (12247-12272), 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, (2023), 25, 11, (12247-12272), 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, (2023), 25, 11, (12247-12272), 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, (2023), 25, 11, (12247-12272), 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, (2023), 25, 11, (12247-12272), 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, (2023), 25, 11, (12247-12272), 10.1007/s10668-022-02506-0)
publisher	Springer Science and Business Media B.V.
publishDate	2025
_version_	1826077648506322944
score	13.244413

Correction: Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development (Environment, Development and Sustainability, (2023), 25, 11, (12247-12272), 10.1007/s10668-022-02506-0)

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