Modelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux

A new unidimensional computational model is developed to simulate a calcination reactor in a Calcium-looping process for thermochemical energy storage in concentrating solar power systems. The proposed reactor is an absorber tube exposed to concentrated solar radiation. This tube is also the riser o...

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Autores principales: Mayra Alvarez Rivero, Diogo Rodrigues, Carla I.C. Pinheiro, João P Cardoso, L. Filipe Mendes
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Lenguaje:EN
Publicado: AIDIC Servizi S.r.l. 2021
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Acceso en línea:https://doaj.org/article/c694ba5001a246779f139d2d829d975c
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spelling oai:doaj.org-article:c694ba5001a246779f139d2d829d975c2021-11-15T21:47:34ZModelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux10.3303/CET21881452283-9216https://doaj.org/article/c694ba5001a246779f139d2d829d975c2021-11-01T00:00:00Zhttps://www.cetjournal.it/index.php/cet/article/view/11938https://doaj.org/toc/2283-9216A new unidimensional computational model is developed to simulate a calcination reactor in a Calcium-looping process for thermochemical energy storage in concentrating solar power systems. The proposed reactor is an absorber tube exposed to concentrated solar radiation. This tube is also the riser of a circulating fluidised bed where the calcination reaction takes place. The proposed heat transfer process models are based on the core-annulus model and the hydrodynamic model is a modified version of the Kunii-Levenspiel model. The model considers the change in the mass flow rate of species and the density change of the phases in the axial direction of the reactor, usually considered constant in the models found in the literature. A higher calcination efficiency, up to 8 p.p., is obtained for the studied reference case when assuming constant density and mass flow rate. Simulations were performed by imposing a solar-driven non-uniform heat flux distribution on the reactor wall. The results show that a 6 m height reactor allows achieving a calcination efficiency of 66% for the reference conditions used. A sensitivity analysis shows that the solids mass flow rate and the inlet bed temperature are the parameters that most affect the calcination process efficiency.Mayra Alvarez RiveroDiogo RodriguesCarla I.C. PinheiroJoão P CardosoL. Filipe MendesAIDIC Servizi S.r.l.articleChemical engineeringTP155-156Computer engineering. Computer hardwareTK7885-7895ENChemical Engineering Transactions, Vol 88 (2021)
institution DOAJ
collection DOAJ
language EN
topic Chemical engineering
TP155-156
Computer engineering. Computer hardware
TK7885-7895
spellingShingle Chemical engineering
TP155-156
Computer engineering. Computer hardware
TK7885-7895
Mayra Alvarez Rivero
Diogo Rodrigues
Carla I.C. Pinheiro
João P Cardoso
L. Filipe Mendes
Modelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux
description A new unidimensional computational model is developed to simulate a calcination reactor in a Calcium-looping process for thermochemical energy storage in concentrating solar power systems. The proposed reactor is an absorber tube exposed to concentrated solar radiation. This tube is also the riser of a circulating fluidised bed where the calcination reaction takes place. The proposed heat transfer process models are based on the core-annulus model and the hydrodynamic model is a modified version of the Kunii-Levenspiel model. The model considers the change in the mass flow rate of species and the density change of the phases in the axial direction of the reactor, usually considered constant in the models found in the literature. A higher calcination efficiency, up to 8 p.p., is obtained for the studied reference case when assuming constant density and mass flow rate. Simulations were performed by imposing a solar-driven non-uniform heat flux distribution on the reactor wall. The results show that a 6 m height reactor allows achieving a calcination efficiency of 66% for the reference conditions used. A sensitivity analysis shows that the solids mass flow rate and the inlet bed temperature are the parameters that most affect the calcination process efficiency.
format article
author Mayra Alvarez Rivero
Diogo Rodrigues
Carla I.C. Pinheiro
João P Cardoso
L. Filipe Mendes
author_facet Mayra Alvarez Rivero
Diogo Rodrigues
Carla I.C. Pinheiro
João P Cardoso
L. Filipe Mendes
author_sort Mayra Alvarez Rivero
title Modelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux
title_short Modelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux
title_full Modelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux
title_fullStr Modelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux
title_full_unstemmed Modelling a Calcium-Looping Fluidised Bed Calcination Reactor with Solar-Driven Heat Flux
title_sort modelling a calcium-looping fluidised bed calcination reactor with solar-driven heat flux
publisher AIDIC Servizi S.r.l.
publishDate 2021
url https://doaj.org/article/c694ba5001a246779f139d2d829d975c
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AT carlaicpinheiro modellingacalciumloopingfluidisedbedcalcinationreactorwithsolardrivenheatflux
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