Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOH

If the interesterification reaction of rapeseed oil with methyl acetate at reactant to oil molar ratio of 18:1 in presence of potassium tert-butoxide in tert-butanol of molar ratio to oil 0.08 is conducted at a temperature of about 35 °C, reaction time for full conversion of oil is shorter than one...

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Main Authors: Kampars Valdis, Gravins Reinis, Lazdovica Kristine, Kampare Ruta
Format: Article
Language:English
Published: EDP Sciences 2019-01-01
Series:E3S Web of Conferences
Online Access:https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/29/e3sconf_icacer2019_02006.pdf
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spelling doaj-a51e682a01d24e1fb549a91063321fab2021-03-02T10:48:01ZengEDP SciencesE3S Web of Conferences2267-12422019-01-011030200610.1051/e3sconf/201910302006e3sconf_icacer2019_02006Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOHKampars ValdisGravins ReinisLazdovica KristineKampare RutaIf the interesterification reaction of rapeseed oil with methyl acetate at reactant to oil molar ratio of 18:1 in presence of potassium tert-butoxide in tert-butanol of molar ratio to oil 0.08 is conducted at a temperature of about 35 °C, reaction time for full conversion of oil is shorter than one hour, while at a temperature of 55 °C it is approximately 15 minutes. Reaction time at the desired temperature has a wide "optimal" range and cannot be an effective variable for the process optimisation. Experimental results at the temperature of 25 °C confirm the pseudo-first order of the reaction, which lowered towards the end of the reaction. The pseudo-first order rate constant was 0.63 min-1. Fuel characteristics of the interesterification reaction mixtures without purification improved with the rising of reaction temperature from 35 °C to 55 °C, however, they fail to meet the requirements of standard EN14214 for biodiesel. Methyl acetate to oil molar ratio 18:1 is too low for obtaining products with kinematic viscosity below 5.0 mm2/s.https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/29/e3sconf_icacer2019_02006.pdf
collection DOAJ
language English
format Article
sources DOAJ
author Kampars Valdis
Gravins Reinis
Lazdovica Kristine
Kampare Ruta
spellingShingle Kampars Valdis
Gravins Reinis
Lazdovica Kristine
Kampare Ruta
Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOH
E3S Web of Conferences
author_facet Kampars Valdis
Gravins Reinis
Lazdovica Kristine
Kampare Ruta
author_sort Kampars Valdis
title Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOH
title_short Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOH
title_full Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOH
title_fullStr Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOH
title_full_unstemmed Effect of Temperature on Interesterification of Rapeseed Oil with Methyl Acetate in Presence of BuOK/BuOH
title_sort effect of temperature on interesterification of rapeseed oil with methyl acetate in presence of buok/buoh
publisher EDP Sciences
series E3S Web of Conferences
issn 2267-1242
publishDate 2019-01-01
description If the interesterification reaction of rapeseed oil with methyl acetate at reactant to oil molar ratio of 18:1 in presence of potassium tert-butoxide in tert-butanol of molar ratio to oil 0.08 is conducted at a temperature of about 35 °C, reaction time for full conversion of oil is shorter than one hour, while at a temperature of 55 °C it is approximately 15 minutes. Reaction time at the desired temperature has a wide "optimal" range and cannot be an effective variable for the process optimisation. Experimental results at the temperature of 25 °C confirm the pseudo-first order of the reaction, which lowered towards the end of the reaction. The pseudo-first order rate constant was 0.63 min-1. Fuel characteristics of the interesterification reaction mixtures without purification improved with the rising of reaction temperature from 35 °C to 55 °C, however, they fail to meet the requirements of standard EN14214 for biodiesel. Methyl acetate to oil molar ratio 18:1 is too low for obtaining products with kinematic viscosity below 5.0 mm2/s.
url https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/29/e3sconf_icacer2019_02006.pdf
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AT lazdovicakristine effectoftemperatureoninteresterificationofrapeseedoilwithmethylacetateinpresenceofbuokbuoh
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