Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral Microchannel

Many microdevices have been tested in order to enhance the interaction between vegetable oil and alcohol to raising the conversion into biodiesel. However, many microdevices have some complexities in manufacturing and/or operation process. Consequently, this work studied numerically the use of a Spi...

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Main Authors: H. Santana, R.L. Amaral, O.P. Taranto
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2015-05-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/5045
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spelling doaj-dfe2a1c4387841b2bb1ba7ef6ef710d22021-02-20T21:10:51ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162015-05-014310.3303/CET1543278Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral MicrochannelH. SantanaR.L. AmaralO.P. TarantoMany microdevices have been tested in order to enhance the interaction between vegetable oil and alcohol to raising the conversion into biodiesel. However, many microdevices have some complexities in manufacturing and/or operation process. Consequently, this work studied numerically the use of a Spiral-micromixer for mixing and reaction of Jatropha curcas oil and ethanol for the production of biodiesel. The simulated microdevices had 200 µm in height and width. The mixing of the fluid was analyzed with Reynolds numbers from 0.67 to 100 and reaction studies were carried out for the same Reynolds numbers and a residence times ranging from 0.2 to 1,000 s. The Spiral-micromixer showed the highest mixing between the oil and ethanol. The highest conversion of vegetable oil in biodiesel was obtained with the T-micromixer (average of 51.8 %) and for the Spiral-micromixer (average of 50 %) for Reynolds number studied. An increment in residence time increased conversion, and the maximum conversion achieved was 98,48 % and 99,99 % for T-micromixer and Spiral-micromixer, respectively. The efficiency of mixing and reaction process can be increased and high conversion ratios obtained using this type of micromixer.https://www.cetjournal.it/index.php/cet/article/view/5045
collection DOAJ
language English
format Article
sources DOAJ
author H. Santana
R.L. Amaral
O.P. Taranto
spellingShingle H. Santana
R.L. Amaral
O.P. Taranto
Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral Microchannel
Chemical Engineering Transactions
author_facet H. Santana
R.L. Amaral
O.P. Taranto
author_sort H. Santana
title Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral Microchannel
title_short Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral Microchannel
title_full Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral Microchannel
title_fullStr Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral Microchannel
title_full_unstemmed Numerical Study of Mixing and Reaction for Biodiesel Production in Spiral Microchannel
title_sort numerical study of mixing and reaction for biodiesel production in spiral microchannel
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2015-05-01
description Many microdevices have been tested in order to enhance the interaction between vegetable oil and alcohol to raising the conversion into biodiesel. However, many microdevices have some complexities in manufacturing and/or operation process. Consequently, this work studied numerically the use of a Spiral-micromixer for mixing and reaction of Jatropha curcas oil and ethanol for the production of biodiesel. The simulated microdevices had 200 µm in height and width. The mixing of the fluid was analyzed with Reynolds numbers from 0.67 to 100 and reaction studies were carried out for the same Reynolds numbers and a residence times ranging from 0.2 to 1,000 s. The Spiral-micromixer showed the highest mixing between the oil and ethanol. The highest conversion of vegetable oil in biodiesel was obtained with the T-micromixer (average of 51.8 %) and for the Spiral-micromixer (average of 50 %) for Reynolds number studied. An increment in residence time increased conversion, and the maximum conversion achieved was 98,48 % and 99,99 % for T-micromixer and Spiral-micromixer, respectively. The efficiency of mixing and reaction process can be increased and high conversion ratios obtained using this type of micromixer.
url https://www.cetjournal.it/index.php/cet/article/view/5045
work_keys_str_mv AT hsantana numericalstudyofmixingandreactionforbiodieselproductioninspiralmicrochannel
AT rlamaral numericalstudyofmixingandreactionforbiodieselproductioninspiralmicrochannel
AT optaranto numericalstudyofmixingandreactionforbiodieselproductioninspiralmicrochannel
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