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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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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