Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed Reactor
This paper presents work on hydrodynamics of several types of biomass mixture in a dual chamber circulating fluidized bed. In designing the CFBreactornecessary to know the distribution of solid particles radially and axially influenced by fluidizing gas velocity, particle size, solid circulation flu...
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2016-01-01
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Series: | MATEC Web of Conferences |
Online Access: | http://dx.doi.org/10.1051/matecconf/20167703004 |
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doaj-af70a2a7cf8649dabe7304013d08db232021-02-02T03:11:15ZengEDP SciencesMATEC Web of Conferences2261-236X2016-01-01770300410.1051/matecconf/20167703004matecconf_icmmr2016_03004Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed ReactorWahyu HaifaDjunaedi ImamAffendi MSugiyatno M. T.This paper presents work on hydrodynamics of several types of biomass mixture in a dual chamber circulating fluidized bed. In designing the CFBreactornecessary to know the distribution of solid particles radially and axially influenced by fluidizing gas velocity, particle size, solid circulation flux, reactor diameter and height of the reactor. These factors will affect pressure drop along the riser of the reaction chamber. Pressure drop is an important factor in the study of hydrodynamics of particle flow. The pressure drop was measured using mathematical model compared to experimental results done on a cold mode. Since it was found that both results were consistent which means that the model can be used to predict the operating parameters of CFB design.http://dx.doi.org/10.1051/matecconf/20167703004 |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Wahyu Haifa Djunaedi Imam Affendi M Sugiyatno M. T. |
spellingShingle |
Wahyu Haifa Djunaedi Imam Affendi M Sugiyatno M. T. Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed Reactor MATEC Web of Conferences |
author_facet |
Wahyu Haifa Djunaedi Imam Affendi M Sugiyatno M. T. |
author_sort |
Wahyu Haifa |
title |
Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed Reactor |
title_short |
Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed Reactor |
title_full |
Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed Reactor |
title_fullStr |
Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed Reactor |
title_full_unstemmed |
Hydrodynamics of Biomass Gasification in a Dual Chamber Circulating Fluidized Bed Reactor |
title_sort |
hydrodynamics of biomass gasification in a dual chamber circulating fluidized bed reactor |
publisher |
EDP Sciences |
series |
MATEC Web of Conferences |
issn |
2261-236X |
publishDate |
2016-01-01 |
description |
This paper presents work on hydrodynamics of several types of biomass mixture in a dual chamber circulating fluidized bed. In designing the CFBreactornecessary to know the distribution of solid particles radially and axially influenced by fluidizing gas velocity, particle size, solid circulation flux, reactor diameter and height of the reactor. These factors will affect pressure drop along the riser of the reaction chamber. Pressure drop is an important factor in the study of hydrodynamics of particle flow. The pressure drop was measured using mathematical model compared to experimental results done on a cold mode. Since it was found that both results were consistent which means that the model can be used to predict the operating parameters of CFB design. |
url |
http://dx.doi.org/10.1051/matecconf/20167703004 |
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