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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EDP Sciences
2019-01-01
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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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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 |
work_keys_str_mv |
AT kamparsvaldis effectoftemperatureoninteresterificationofrapeseedoilwithmethylacetateinpresenceofbuokbuoh AT gravinsreinis effectoftemperatureoninteresterificationofrapeseedoilwithmethylacetateinpresenceofbuokbuoh AT lazdovicakristine effectoftemperatureoninteresterificationofrapeseedoilwithmethylacetateinpresenceofbuokbuoh AT kampareruta effectoftemperatureoninteresterificationofrapeseedoilwithmethylacetateinpresenceofbuokbuoh |
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1724236115208044544 |