Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with Biomass

This paper specifies the mathematical and physical modelling of the iron sintering process in laboratory conditions. The aim is to get the simplest approach (using thermodynamic software “HSC Chemistry”, version 9, Outokumpu Research Oy, Pori, Finland) that allows one to predict...

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Main Authors: Jaroslav Legemza, Mária Fröhlichová, Róbert Findorák, Martina Džupková
Format: Article
Language:English
Published: MDPI AG 2019-09-01
Series:Metals
Subjects:
Online Access:https://www.mdpi.com/2075-4701/9/9/1010
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author Jaroslav Legemza
Mária Fröhlichová
Róbert Findorák
Martina Džupková
author_facet Jaroslav Legemza
Mária Fröhlichová
Róbert Findorák
Martina Džupková
author_sort Jaroslav Legemza
collection DOAJ
description This paper specifies the mathematical and physical modelling of the iron sintering process in laboratory conditions. The aim is to get the simplest approach (using thermodynamic software “HSC Chemistry”, version 9, Outokumpu Research Oy, Pori, Finland) that allows one to predict the output parameters based on the initial composition analysis. As a part of the application of mathematical modelling, a mass and thermal balance of combustion of carbonaceous fuels (including biomass) and a mass and thermal balance of high-temperature sintering of an agglomeration charge were determined. The objective of the paper was to point out the advantages of modelling using thermodynamic software and apply the results into a simulation of the sintering process. The outcome of mathematical modelling correlates to the outcome of physical modelling for fuel combustion and the agglomerate production in a laboratory sintering pan. The energy required to reach the desired sintering temperatures and acquire the standard quality of agglomerate was calculated using 4.97% of coke breeze. In a real experiment with the laboratory sintering pan, 4.35% of coke was used. When a biomass fuel with a lower calorific value (lignin) is used in the agglomeration charge, the amount of fuel has to be increased to 5.52% (with 20% substitution of coke). This paper also aimed at predicting methodological tools and defining thermodynamic conditions for creating an interactive simulation. In addition, kinetics should be considered to improve the predicting capabilities of the current model and therefore in further research it will be required to optimise the computational program pursuant to the results of the kinetics experiments.
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spelling doaj.art-2a53c0d5a08347a48b2839f66d773ce42022-12-22T02:00:29ZengMDPI AGMetals2075-47012019-09-0199101010.3390/met9091010met9091010Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with BiomassJaroslav Legemza0Mária Fröhlichová1Róbert Findorák2Martina Džupková3Faculty of Materials, Metallurgy and Recycling, Technical University of Košice, Letná 9, 04200 Košice, SlovakiaFaculty of Materials, Metallurgy and Recycling, Technical University of Košice, Letná 9, 04200 Košice, SlovakiaFaculty of Materials, Metallurgy and Recycling, Technical University of Košice, Letná 9, 04200 Košice, SlovakiaFaculty of Materials, Metallurgy and Recycling, Technical University of Košice, Letná 9, 04200 Košice, SlovakiaThis paper specifies the mathematical and physical modelling of the iron sintering process in laboratory conditions. The aim is to get the simplest approach (using thermodynamic software “HSC Chemistry”, version 9, Outokumpu Research Oy, Pori, Finland) that allows one to predict the output parameters based on the initial composition analysis. As a part of the application of mathematical modelling, a mass and thermal balance of combustion of carbonaceous fuels (including biomass) and a mass and thermal balance of high-temperature sintering of an agglomeration charge were determined. The objective of the paper was to point out the advantages of modelling using thermodynamic software and apply the results into a simulation of the sintering process. The outcome of mathematical modelling correlates to the outcome of physical modelling for fuel combustion and the agglomerate production in a laboratory sintering pan. The energy required to reach the desired sintering temperatures and acquire the standard quality of agglomerate was calculated using 4.97% of coke breeze. In a real experiment with the laboratory sintering pan, 4.35% of coke was used. When a biomass fuel with a lower calorific value (lignin) is used in the agglomeration charge, the amount of fuel has to be increased to 5.52% (with 20% substitution of coke). This paper also aimed at predicting methodological tools and defining thermodynamic conditions for creating an interactive simulation. In addition, kinetics should be considered to improve the predicting capabilities of the current model and therefore in further research it will be required to optimise the computational program pursuant to the results of the kinetics experiments.https://www.mdpi.com/2075-4701/9/9/1010agglomeratecarbon fuelcoke breezebiomassligninmodellingmass-thermal balancetemperaturesintering
spellingShingle Jaroslav Legemza
Mária Fröhlichová
Róbert Findorák
Martina Džupková
Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with Biomass
Metals
agglomerate
carbon fuel
coke breeze
biomass
lignin
modelling
mass-thermal balance
temperature
sintering
title Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with Biomass
title_full Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with Biomass
title_fullStr Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with Biomass
title_full_unstemmed Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with Biomass
title_short Modelling of Mass and Thermal Balance and Simulation of Iron Sintering Process with Biomass
title_sort modelling of mass and thermal balance and simulation of iron sintering process with biomass
topic agglomerate
carbon fuel
coke breeze
biomass
lignin
modelling
mass-thermal balance
temperature
sintering
url https://www.mdpi.com/2075-4701/9/9/1010
work_keys_str_mv AT jaroslavlegemza modellingofmassandthermalbalanceandsimulationofironsinteringprocesswithbiomass
AT mariafrohlichova modellingofmassandthermalbalanceandsimulationofironsinteringprocesswithbiomass
AT robertfindorak modellingofmassandthermalbalanceandsimulationofironsinteringprocesswithbiomass
AT martinadzupkova modellingofmassandthermalbalanceandsimulationofironsinteringprocesswithbiomass