Non-isothermal effectiveness factors in thermo-chemical char conversion

Modeling heterogeneous combustion and gasification at large or industry scale is important in ongoing research and development activities. These simulations rely on comprehensive, accurate, and efficient solid conversion models. Pore diffusion is an important sub-process of gas–solid reactions and i...

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Main Authors: Markus Bösenhofer, Michael Harasek
Format: Article
Language:English
Published: KeAi Communications Co., Ltd. 2021-01-01
Series:Carbon Resources Conversion
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2588913321000120
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spelling doaj-2423fae943114755b21b7b61330eb0462021-04-02T17:46:35ZengKeAi Communications Co., Ltd.Carbon Resources Conversion2588-91332021-01-0144754Non-isothermal effectiveness factors in thermo-chemical char conversionMarkus Bösenhofer0Michael Harasek1TU Wien, Institute of Chemical, Environmental and Bioscience Engineering, Getreidemarkt 9/166, 1060 Vienna, Austria; K1-MET GmbH, Area 4 - Simulation and Analyses, Stahlstraße 14, 4020 Linz, Austria; Corresponding author at: TU Wien, Institute of Chemical, Environmental and Bioscience Engineering, Getreidemarkt 9/166, 1060 Vienna, Austria.TU Wien, Institute of Chemical, Environmental and Bioscience Engineering, Getreidemarkt 9/166, 1060 Vienna, AustriaModeling heterogeneous combustion and gasification at large or industry scale is important in ongoing research and development activities. These simulations rely on comprehensive, accurate, and efficient solid conversion models. Pore diffusion is an important sub-process of gas–solid reactions and is often approximated by effectiveness factors. Analytic expressions for isothermal effectiveness factors are usually used, due to the numerical effort of determining non-isothermal ones. The consequences of this simplification are evaluated by determining non-isothermal effectiveness factors for typical combustion conditions for the reactions of carbon with O2,CO2,H2O, and H2. The results show that exothermal reaction rates are under-estimated, while endothermal are over-estimated at low and intermediate temperatures for Thiele moduli between 0.1 and 100. In addition, the reaction zone relocates towards the outer particle layers under these conditions. Cross-sensitivity effects between the four reactions are neglected in this study. A reasonable approximation is the superposition of the individual reactions, because the oxidation reaction is dominant under typical combustion conditions.http://www.sciencedirect.com/science/article/pii/S2588913321000120Reaction-diffusion equationNon-isothermal char conversionGas-solid reactionsShooting methodNon-linear boundary value problem
collection DOAJ
language English
format Article
sources DOAJ
author Markus Bösenhofer
Michael Harasek
spellingShingle Markus Bösenhofer
Michael Harasek
Non-isothermal effectiveness factors in thermo-chemical char conversion
Carbon Resources Conversion
Reaction-diffusion equation
Non-isothermal char conversion
Gas-solid reactions
Shooting method
Non-linear boundary value problem
author_facet Markus Bösenhofer
Michael Harasek
author_sort Markus Bösenhofer
title Non-isothermal effectiveness factors in thermo-chemical char conversion
title_short Non-isothermal effectiveness factors in thermo-chemical char conversion
title_full Non-isothermal effectiveness factors in thermo-chemical char conversion
title_fullStr Non-isothermal effectiveness factors in thermo-chemical char conversion
title_full_unstemmed Non-isothermal effectiveness factors in thermo-chemical char conversion
title_sort non-isothermal effectiveness factors in thermo-chemical char conversion
publisher KeAi Communications Co., Ltd.
series Carbon Resources Conversion
issn 2588-9133
publishDate 2021-01-01
description Modeling heterogeneous combustion and gasification at large or industry scale is important in ongoing research and development activities. These simulations rely on comprehensive, accurate, and efficient solid conversion models. Pore diffusion is an important sub-process of gas–solid reactions and is often approximated by effectiveness factors. Analytic expressions for isothermal effectiveness factors are usually used, due to the numerical effort of determining non-isothermal ones. The consequences of this simplification are evaluated by determining non-isothermal effectiveness factors for typical combustion conditions for the reactions of carbon with O2,CO2,H2O, and H2. The results show that exothermal reaction rates are under-estimated, while endothermal are over-estimated at low and intermediate temperatures for Thiele moduli between 0.1 and 100. In addition, the reaction zone relocates towards the outer particle layers under these conditions. Cross-sensitivity effects between the four reactions are neglected in this study. A reasonable approximation is the superposition of the individual reactions, because the oxidation reaction is dominant under typical combustion conditions.
topic Reaction-diffusion equation
Non-isothermal char conversion
Gas-solid reactions
Shooting method
Non-linear boundary value problem
url http://www.sciencedirect.com/science/article/pii/S2588913321000120
work_keys_str_mv AT markusbosenhofer nonisothermaleffectivenessfactorsinthermochemicalcharconversion
AT michaelharasek nonisothermaleffectivenessfactorsinthermochemicalcharconversion
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