Production of Biodiesel from Waste Vegetable Oil via KM Micromixer

The production of biodiesel from waste vegetable oils through its pretreatment followed by transesterification process in presence of methanol was investigated using a KM micromixer reactor. The parameters affecting biodiesel production process such as alcohol to oil molar ratio, catalyst concentrat...

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Main Authors: M. F. Elkady, Ahmed Zaatout, Ola Balbaa
Format: Article
Language:English
Published: Hindawi Limited 2015-01-01
Series:Journal of Chemistry
Online Access:http://dx.doi.org/10.1155/2015/630168
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spelling doaj-41fe387d9ff343d5b34cec4c19441e112020-11-24T21:06:31ZengHindawi LimitedJournal of Chemistry2090-90632090-90712015-01-01201510.1155/2015/630168630168Production of Biodiesel from Waste Vegetable Oil via KM MicromixerM. F. Elkady0Ahmed Zaatout1Ola Balbaa2Chemical and Petrochemical Engineering Department, Egypt-Japan University of Science and Technology, New Borg El Arab City, Alexandria 21934, EgyptChemical Engineering Department, Faculty of Engineering, Alexandria University, Alexandria 21544, EgyptChemical Engineering Department, Faculty of Engineering, Alexandria University, Alexandria 21544, EgyptThe production of biodiesel from waste vegetable oils through its pretreatment followed by transesterification process in presence of methanol was investigated using a KM micromixer reactor. The parameters affecting biodiesel production process such as alcohol to oil molar ratio, catalyst concentration, the presence of tetrahydrofuran (THF) as a cosolvent, and the volumetric flow rates of inlet fluids were optimized. The properties of the produced biodiesel were compared with its parent waste oil through different characterization techniques. The presence of methyl ester groups at the produced biodiesel was confirmed using both the gas chromatography-mass spectrometry (GC-MS) and the infrared spectroscopy (FT-IR). Moreover, the thermal analysis of the produced biodiesel and the comparable waste oil indicated that the product after the transesterification process began to vaporize at 120°C which makes it lighter than its parent oil which started to vaporize at around 300°C. The maximum biodiesel production yield of 97% was recorded using 12 : 1 methanol to oil molar ratio in presence of both 1% NaOH and THF/methanol volume ratio 0.3 at 60 mL/h flow rate.http://dx.doi.org/10.1155/2015/630168
collection DOAJ
language English
format Article
sources DOAJ
author M. F. Elkady
Ahmed Zaatout
Ola Balbaa
spellingShingle M. F. Elkady
Ahmed Zaatout
Ola Balbaa
Production of Biodiesel from Waste Vegetable Oil via KM Micromixer
Journal of Chemistry
author_facet M. F. Elkady
Ahmed Zaatout
Ola Balbaa
author_sort M. F. Elkady
title Production of Biodiesel from Waste Vegetable Oil via KM Micromixer
title_short Production of Biodiesel from Waste Vegetable Oil via KM Micromixer
title_full Production of Biodiesel from Waste Vegetable Oil via KM Micromixer
title_fullStr Production of Biodiesel from Waste Vegetable Oil via KM Micromixer
title_full_unstemmed Production of Biodiesel from Waste Vegetable Oil via KM Micromixer
title_sort production of biodiesel from waste vegetable oil via km micromixer
publisher Hindawi Limited
series Journal of Chemistry
issn 2090-9063
2090-9071
publishDate 2015-01-01
description The production of biodiesel from waste vegetable oils through its pretreatment followed by transesterification process in presence of methanol was investigated using a KM micromixer reactor. The parameters affecting biodiesel production process such as alcohol to oil molar ratio, catalyst concentration, the presence of tetrahydrofuran (THF) as a cosolvent, and the volumetric flow rates of inlet fluids were optimized. The properties of the produced biodiesel were compared with its parent waste oil through different characterization techniques. The presence of methyl ester groups at the produced biodiesel was confirmed using both the gas chromatography-mass spectrometry (GC-MS) and the infrared spectroscopy (FT-IR). Moreover, the thermal analysis of the produced biodiesel and the comparable waste oil indicated that the product after the transesterification process began to vaporize at 120°C which makes it lighter than its parent oil which started to vaporize at around 300°C. The maximum biodiesel production yield of 97% was recorded using 12 : 1 methanol to oil molar ratio in presence of both 1% NaOH and THF/methanol volume ratio 0.3 at 60 mL/h flow rate.
url http://dx.doi.org/10.1155/2015/630168
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