Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activity

A kinetic model for direct coal liquefaction at low temperature in the presence of a magnetite nano-catalyst was developed. The model took into account the iron oxide catalyst transformation into its active state as well as the process of reactive dissolution of coal at the reduced temperatures. The...

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Main Authors: Ethan Gabriel Hammond, Shaheen Amed Faizal Moonsamy, David Lokhat, Milan Carsky
Format: Article
Language:English
Published: Elsevier 2021-07-01
Series:South African Journal of Chemical Engineering
Online Access:http://www.sciencedirect.com/science/article/pii/S1026918521000172
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spelling doaj-54489b4ec2ee410799323710f2bc92da2021-07-09T04:42:19ZengElsevierSouth African Journal of Chemical Engineering1026-91852021-07-01373745Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activityEthan Gabriel Hammond0Shaheen Amed Faizal Moonsamy1David Lokhat2Milan Carsky3Corresponding author.; Reactor Technology Research Group, School of Engineering, University of KwaZulu-Natal, Durban 4041, South AfricaReactor Technology Research Group, School of Engineering, University of KwaZulu-Natal, Durban 4041, South AfricaReactor Technology Research Group, School of Engineering, University of KwaZulu-Natal, Durban 4041, South AfricaReactor Technology Research Group, School of Engineering, University of KwaZulu-Natal, Durban 4041, South AfricaA kinetic model for direct coal liquefaction at low temperature in the presence of a magnetite nano-catalyst was developed. The model took into account the iron oxide catalyst transformation into its active state as well as the process of reactive dissolution of coal at the reduced temperatures. The validity of the model was tested by performing a regression on experimentally obtained data for the direct coal liquefaction process. The experiments were performed in a high-pressure batch reactor, with medium to low ranking coal, using synthesised magnetite nano-catalysts and within the temperature range of 240 °C to 320 °C. This temperature range is known to be below that required for thermolysis of the coal. The model was able to qualitatively capture the general trends of the experimental data. The regression indicated that the depolymerisation reactions of the dissolved moieties directly into key products occur more rapidly than the reactions of key product groups, which is a typical occurrence in lower rank coals.http://www.sciencedirect.com/science/article/pii/S1026918521000172
collection DOAJ
language English
format Article
sources DOAJ
author Ethan Gabriel Hammond
Shaheen Amed Faizal Moonsamy
David Lokhat
Milan Carsky
spellingShingle Ethan Gabriel Hammond
Shaheen Amed Faizal Moonsamy
David Lokhat
Milan Carsky
Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activity
South African Journal of Chemical Engineering
author_facet Ethan Gabriel Hammond
Shaheen Amed Faizal Moonsamy
David Lokhat
Milan Carsky
author_sort Ethan Gabriel Hammond
title Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activity
title_short Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activity
title_full Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activity
title_fullStr Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activity
title_full_unstemmed Kinetic modelling of low temperature direct coal liquefaction: Consideration of dynamic catalyst activity
title_sort kinetic modelling of low temperature direct coal liquefaction: consideration of dynamic catalyst activity
publisher Elsevier
series South African Journal of Chemical Engineering
issn 1026-9185
publishDate 2021-07-01
description A kinetic model for direct coal liquefaction at low temperature in the presence of a magnetite nano-catalyst was developed. The model took into account the iron oxide catalyst transformation into its active state as well as the process of reactive dissolution of coal at the reduced temperatures. The validity of the model was tested by performing a regression on experimentally obtained data for the direct coal liquefaction process. The experiments were performed in a high-pressure batch reactor, with medium to low ranking coal, using synthesised magnetite nano-catalysts and within the temperature range of 240 °C to 320 °C. This temperature range is known to be below that required for thermolysis of the coal. The model was able to qualitatively capture the general trends of the experimental data. The regression indicated that the depolymerisation reactions of the dissolved moieties directly into key products occur more rapidly than the reactions of key product groups, which is a typical occurrence in lower rank coals.
url http://www.sciencedirect.com/science/article/pii/S1026918521000172
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AT davidlokhat kineticmodellingoflowtemperaturedirectcoalliquefactionconsiderationofdynamiccatalystactivity
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