Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hour
Rice husk is one of the most abundant biomass wastes in Indonesia. One way to convert it into an alternative source of energy is biomass gasification. This is a thermochemical process which converts biomass feedstock into fuel gas or chemical feedstock gas (producer gas). The gasification type w...
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Format: | Article |
Language: | English |
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Universitas Indonesia
2016-12-01
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Series: | International Journal of Technology |
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Online Access: | http://ijtech.eng.ui.ac.id/article/view/275 |
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author | Hafif Dafiqurrohman Adi Surjosatyo Felly Rihlat Gibran |
author_facet | Hafif Dafiqurrohman Adi Surjosatyo Felly Rihlat Gibran |
author_sort | Hafif Dafiqurrohman |
collection | DOAJ |
description | Rice husk is one of the
most abundant biomass wastes in Indonesia. One way to convert it into an
alternative source of energy is biomass gasification. This is a thermochemical
process which converts biomass feedstock into fuel gas or chemical feedstock
gas (producer gas). The gasification type which is developed in this study is
fixed bed downdraft type due to its low tar content and compatibility in
microscale implementation. One major problem with the implemented biomass
gasification reactor was ruggedness of the partial oxidation process due to the
absence of air in the reactor’s middle section, which consequently affected the
pyrolysis zone. Several experiments were conducted previously using coconut
shells and rice husks as solid feedstock, where an equivalence ratio (ER) of
0.4 was obtained. Therefore, in order to optimize the pyrolysis zone, the
modification conducted involves adding a circular air intake into the gasifier.
Experiments were conducted in a pyrolysis temperature range of 300–700oC
with ER variation of 0.19, 0.24, 0.27 and 0.31. The results show that a good
quality producer gas is produced at an ER value of 0.24. This value shows a
promising result because the ER value of biomass gasification standard is 0.25. |
first_indexed | 2024-04-11T02:15:36Z |
format | Article |
id | doaj.art-f546cea608494b4098ec9c57fbfc902a |
institution | Directory Open Access Journal |
issn | 2086-9614 2087-2100 |
language | English |
last_indexed | 2024-04-11T02:15:36Z |
publishDate | 2016-12-01 |
publisher | Universitas Indonesia |
record_format | Article |
series | International Journal of Technology |
spelling | doaj.art-f546cea608494b4098ec9c57fbfc902a2023-01-03T01:24:13ZengUniversitas IndonesiaInternational Journal of Technology2086-96142087-21002016-12-01781352136110.14716/ijtech.v7i8.275275Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hourHafif Dafiqurrohman0Adi Surjosatyo1Felly Rihlat Gibran2Department of Mechanical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI Depok, Depok 16424, Indonesia. Tropical Renewable Energy Center, Faculty of Engineering, Universitas IndDepartment of Mechanical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI Depok, Depok 16424, Indonesia. Tropical Renewable Energy Center, Faculty of Engineering, Universitas IndoDepartment of Mechanical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI Depok, Depok 16424, IndonesiaRice husk is one of the most abundant biomass wastes in Indonesia. One way to convert it into an alternative source of energy is biomass gasification. This is a thermochemical process which converts biomass feedstock into fuel gas or chemical feedstock gas (producer gas). The gasification type which is developed in this study is fixed bed downdraft type due to its low tar content and compatibility in microscale implementation. One major problem with the implemented biomass gasification reactor was ruggedness of the partial oxidation process due to the absence of air in the reactor’s middle section, which consequently affected the pyrolysis zone. Several experiments were conducted previously using coconut shells and rice husks as solid feedstock, where an equivalence ratio (ER) of 0.4 was obtained. Therefore, in order to optimize the pyrolysis zone, the modification conducted involves adding a circular air intake into the gasifier. Experiments were conducted in a pyrolysis temperature range of 300–700oC with ER variation of 0.19, 0.24, 0.27 and 0.31. The results show that a good quality producer gas is produced at an ER value of 0.24. This value shows a promising result because the ER value of biomass gasification standard is 0.25.http://ijtech.eng.ui.ac.id/article/view/275Biomass gasificationCircular air intakeFixed bed downdraftOptimized pyrolysis zoneRice husk |
spellingShingle | Hafif Dafiqurrohman Adi Surjosatyo Felly Rihlat Gibran Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hour International Journal of Technology Biomass gasification Circular air intake Fixed bed downdraft Optimized pyrolysis zone Rice husk |
title | Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hour |
title_full | Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hour |
title_fullStr | Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hour |
title_full_unstemmed | Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hour |
title_short | Air Intake Modification for Pyrolysis Optimization on Rice Husk Fixed Bed Downdraft Gasifier with Maximum Capacity of 30 Kg/hour |
title_sort | air intake modification for pyrolysis optimization on rice husk fixed bed downdraft gasifier with maximum capacity of 30 kg hour |
topic | Biomass gasification Circular air intake Fixed bed downdraft Optimized pyrolysis zone Rice husk |
url | http://ijtech.eng.ui.ac.id/article/view/275 |
work_keys_str_mv | AT hafifdafiqurrohman airintakemodificationforpyrolysisoptimizationonricehuskfixedbeddowndraftgasifierwithmaximumcapacityof30kghour AT adisurjosatyo airintakemodificationforpyrolysisoptimizationonricehuskfixedbeddowndraftgasifierwithmaximumcapacityof30kghour AT fellyrihlatgibran airintakemodificationforpyrolysisoptimizationonricehuskfixedbeddowndraftgasifierwithmaximumcapacityof30kghour |