Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber

Colombian panela agroindustry uses bagasse, a milling byproduct, as fuel for fixed bed furnaces to obtain the energ y required in the panela production process. At the moment, the Ward-Cimpa combustion chamber is the most efficient furnace available; but, it is empirically d...

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Main Authors: Oscar Mendieta Menjura, Zamir Sanchez
Format: Article
Language:Spanish
Published: Corporación Colombiana de Investigación Agropecuaria (Corpoica) 2014-07-01
Series:Ciencia y Tecnología Agropecuaria
Subjects:
Online Access:http://revista.corpoica.org.co/index.php/revista/article/view/355/383
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spelling doaj-53eb1b5b5440404d827d0b6cb8557e542020-11-25T03:15:48ZspaCorporación Colombiana de Investigación Agropecuaria (Corpoica)Ciencia y Tecnología Agropecuaria0122-87062014-07-0115213315110.21930/rcta.vol15_num2_art:355Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamberOscar Mendieta Menjura0Zamir Sanchez1CorpoicaUniversidad Industrial de SantanderColombian panela agroindustry uses bagasse, a milling byproduct, as fuel for fixed bed furnaces to obtain the energ y required in the panela production process. At the moment, the Ward-Cimpa combustion chamber is the most efficient furnace available; but, it is empirically designed and constructed, since detailed mathematical models describing the combustion of biomass in these furnaces are not reported. This situation leads in many cases to inappropriate designs, which generate losses of 10% by incomplete combustion and of 40% unburned material. This research proposes a mathematical model -which involves kinetic expressions- for drying, devolatilization and oxidation of volatiles and carbonized material stages, based on the mass, energ y and momentum balances for the solid and gaseous phases. The kinetic parameters were fitted to expermental data using the stochastic optimization algorithm: simulated annealing. The fitted model describes with an average error of 11%, the combustion rate, bed temperature and CO2 and O2concentration in the flue gas, depending on the primary air flow and the moisture mass fraction. However, the model overestimated the CO concentration by about 50%.http://revista.corpoica.org.co/index.php/revista/article/view/355/383biomass combustionmoisture contentair flowfixed bedpanela
collection DOAJ
language Spanish
format Article
sources DOAJ
author Oscar Mendieta Menjura
Zamir Sanchez
spellingShingle Oscar Mendieta Menjura
Zamir Sanchez
Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber
Ciencia y Tecnología Agropecuaria
biomass combustion
moisture content
air flow
fixed bed
panela
author_facet Oscar Mendieta Menjura
Zamir Sanchez
author_sort Oscar Mendieta Menjura
title Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber
title_short Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber
title_full Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber
title_fullStr Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber
title_full_unstemmed Setting of a mathematical model for the sugarcane bagasse combustion in a Ward-Cimpa chamber
title_sort setting of a mathematical model for the sugarcane bagasse combustion in a ward-cimpa chamber
publisher Corporación Colombiana de Investigación Agropecuaria (Corpoica)
series Ciencia y Tecnología Agropecuaria
issn 0122-8706
publishDate 2014-07-01
description Colombian panela agroindustry uses bagasse, a milling byproduct, as fuel for fixed bed furnaces to obtain the energ y required in the panela production process. At the moment, the Ward-Cimpa combustion chamber is the most efficient furnace available; but, it is empirically designed and constructed, since detailed mathematical models describing the combustion of biomass in these furnaces are not reported. This situation leads in many cases to inappropriate designs, which generate losses of 10% by incomplete combustion and of 40% unburned material. This research proposes a mathematical model -which involves kinetic expressions- for drying, devolatilization and oxidation of volatiles and carbonized material stages, based on the mass, energ y and momentum balances for the solid and gaseous phases. The kinetic parameters were fitted to expermental data using the stochastic optimization algorithm: simulated annealing. The fitted model describes with an average error of 11%, the combustion rate, bed temperature and CO2 and O2concentration in the flue gas, depending on the primary air flow and the moisture mass fraction. However, the model overestimated the CO concentration by about 50%.
topic biomass combustion
moisture content
air flow
fixed bed
panela
url http://revista.corpoica.org.co/index.php/revista/article/view/355/383
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