CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed Dryer

Tea processing is basically distinguished into three types which black tea, green tea, and oolong tea. Green tea is processed by heating and drying the leaves. Green tea factories in Indonesia are generally using the process of drying by panning the leaves. It is more recommended to use the fluidiza...

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Main Authors: Yohana Eflita, Prasetya Nugraha Afif, Eva Diana Ade, Mahawan Ilham, Nugroho Sri
Format: Article
Language:English
Published: EDP Sciences 2018-01-01
Series:E3S Web of Conferences
Online Access:https://doi.org/10.1051/e3sconf/20183101009
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spelling doaj-aecf55c6143147afbe58bb50eaf6731b2021-04-02T14:46:48ZengEDP SciencesE3S Web of Conferences2267-12422018-01-01310100910.1051/e3sconf/20183101009e3sconf_icenis2018_01009CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed DryerYohana EflitaPrasetya Nugraha AfifEva Diana AdeMahawan IlhamNugroho SriTea processing is basically distinguished into three types which black tea, green tea, and oolong tea. Green tea is processed by heating and drying the leaves. Green tea factories in Indonesia are generally using the process of drying by panning the leaves. It is more recommended to use the fluidization process to speed up the drying process as the quality of the tea can be maintained. Bubbling fluidization is expected to occur in this research. It is a process of bubbles are formed in the fluidization. The effectiveness of the drying process in a fluidized bed dryer machine needs to be improved by using a CFD simulation method to proof that umf < u < ut, where the average velocity value is limited by the minimum and the maximum velocity of the calculation the experimental data. The minimum and the maximum velocity value of the fluidization is 0.96 m/s and 8.2 m/s. The result of the simulation obtained that the average velocity of the upper bed part is 1.81 m/s. From the results obtained, it can be concluded that the calculation and the simulation data is in accordance with the condition of bubbling fluidization in fluidized bed dryer.https://doi.org/10.1051/e3sconf/20183101009
collection DOAJ
language English
format Article
sources DOAJ
author Yohana Eflita
Prasetya Nugraha Afif
Eva Diana Ade
Mahawan Ilham
Nugroho Sri
spellingShingle Yohana Eflita
Prasetya Nugraha Afif
Eva Diana Ade
Mahawan Ilham
Nugroho Sri
CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed Dryer
E3S Web of Conferences
author_facet Yohana Eflita
Prasetya Nugraha Afif
Eva Diana Ade
Mahawan Ilham
Nugroho Sri
author_sort Yohana Eflita
title CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed Dryer
title_short CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed Dryer
title_full CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed Dryer
title_fullStr CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed Dryer
title_full_unstemmed CFD Analysis to Calculate the Optimal Air Velocity in Drying Green Tea Process Using Fluidized Bed Dryer
title_sort cfd analysis to calculate the optimal air velocity in drying green tea process using fluidized bed dryer
publisher EDP Sciences
series E3S Web of Conferences
issn 2267-1242
publishDate 2018-01-01
description Tea processing is basically distinguished into three types which black tea, green tea, and oolong tea. Green tea is processed by heating and drying the leaves. Green tea factories in Indonesia are generally using the process of drying by panning the leaves. It is more recommended to use the fluidization process to speed up the drying process as the quality of the tea can be maintained. Bubbling fluidization is expected to occur in this research. It is a process of bubbles are formed in the fluidization. The effectiveness of the drying process in a fluidized bed dryer machine needs to be improved by using a CFD simulation method to proof that umf < u < ut, where the average velocity value is limited by the minimum and the maximum velocity of the calculation the experimental data. The minimum and the maximum velocity value of the fluidization is 0.96 m/s and 8.2 m/s. The result of the simulation obtained that the average velocity of the upper bed part is 1.81 m/s. From the results obtained, it can be concluded that the calculation and the simulation data is in accordance with the condition of bubbling fluidization in fluidized bed dryer.
url https://doi.org/10.1051/e3sconf/20183101009
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