Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes

Abstract A comprehensive computational fluid dynamic (CFD) model of CEES‐developed polyethylenimine impregnated protonated titanate nanotubes (PEI‐PTNTs) was developed using the Multiphase Flow with Interphase eXchanges (MFiX) package to evaluate the performance of the PEI‐PTNTs in a 1‐MW pilot‐scal...

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Main Authors: Hyoung‐Chul Kim, Hongbo Du, Raghava R. Kommalapati, Ziaul Huque, Xinhua Shen
Format: Article
Language:English
Published: Wiley 2020-07-01
Series:Energy Science & Engineering
Subjects:
Online Access:https://doi.org/10.1002/ese3.665
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author Hyoung‐Chul Kim
Hongbo Du
Raghava R. Kommalapati
Ziaul Huque
Xinhua Shen
author_facet Hyoung‐Chul Kim
Hongbo Du
Raghava R. Kommalapati
Ziaul Huque
Xinhua Shen
author_sort Hyoung‐Chul Kim
collection DOAJ
description Abstract A comprehensive computational fluid dynamic (CFD) model of CEES‐developed polyethylenimine impregnated protonated titanate nanotubes (PEI‐PTNTs) was developed using the Multiphase Flow with Interphase eXchanges (MFiX) package to evaluate the performance of the PEI‐PTNTs in a 1‐MW pilot‐scale carbon capture reactor developed by the National Energy Technology Laboratory (NETL). In this CFD model, the momentum, continuity, and energy transport equations were integrated with the first‐order chemistry model for chemical kinetics of heterogeneous reactions to predict the adsorption of CO2 onto amine‐based sorbent particles and the reactor temperature. Based on the amount of the CO2 adsorption obtained in the small‐scale experiment, the coefficients for the chemical reaction equations of PEI‐PTNTs are adjusted. The adjusted PEI‐PTNTs model is applied to the simplified numerical model of 1‐MW pilot‐scale carbon capture system, which is calibrated through the comparison between our simulation results and the results provided by NETL. This calibrated CFD model is used for selecting the optimized flow rate of the gas phase. Our study shows that the optimized gas flow rate to absorb 100% CO2 without loss is 1.5 kg/s, but if higher absorption rate is preferable despite some loss of CO2 absorption in the reactor, a higher flow rate than 1.5 kg/s can be selected.
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spelling doaj.art-9f54a53f59214b72b3537d72a59b23b42022-12-21T19:42:19ZengWileyEnergy Science & Engineering2050-05052020-07-01872311232110.1002/ese3.665Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubesHyoung‐Chul Kim0Hongbo Du1Raghava R. Kommalapati2Ziaul Huque3Xinhua Shen4Center for Energy and Environmental Sustainability (CEES) Prairie View A&M University Prairie View TX USACenter for Energy and Environmental Sustainability (CEES) Prairie View A&M University Prairie View TX USACenter for Energy and Environmental Sustainability (CEES) Prairie View A&M University Prairie View TX USACenter for Energy and Environmental Sustainability (CEES) Prairie View A&M University Prairie View TX USADepartment of Earth and Environmental Sciences University of Northern Iowa Cedar Falls IA USAAbstract A comprehensive computational fluid dynamic (CFD) model of CEES‐developed polyethylenimine impregnated protonated titanate nanotubes (PEI‐PTNTs) was developed using the Multiphase Flow with Interphase eXchanges (MFiX) package to evaluate the performance of the PEI‐PTNTs in a 1‐MW pilot‐scale carbon capture reactor developed by the National Energy Technology Laboratory (NETL). In this CFD model, the momentum, continuity, and energy transport equations were integrated with the first‐order chemistry model for chemical kinetics of heterogeneous reactions to predict the adsorption of CO2 onto amine‐based sorbent particles and the reactor temperature. Based on the amount of the CO2 adsorption obtained in the small‐scale experiment, the coefficients for the chemical reaction equations of PEI‐PTNTs are adjusted. The adjusted PEI‐PTNTs model is applied to the simplified numerical model of 1‐MW pilot‐scale carbon capture system, which is calibrated through the comparison between our simulation results and the results provided by NETL. This calibrated CFD model is used for selecting the optimized flow rate of the gas phase. Our study shows that the optimized gas flow rate to absorb 100% CO2 without loss is 1.5 kg/s, but if higher absorption rate is preferable despite some loss of CO2 absorption in the reactor, a higher flow rate than 1.5 kg/s can be selected.https://doi.org/10.1002/ese3.665computational fluid dynamic simulationchemical reactionsMFiXsolid amine‐based carbon capturetitanate nanotubes
spellingShingle Hyoung‐Chul Kim
Hongbo Du
Raghava R. Kommalapati
Ziaul Huque
Xinhua Shen
Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes
Energy Science & Engineering
computational fluid dynamic simulation
chemical reactions
MFiX
solid amine‐based carbon capture
titanate nanotubes
title Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes
title_full Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes
title_fullStr Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes
title_full_unstemmed Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes
title_short Computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes
title_sort computational fluid dynamic simulation modeling of carbon capture using polyethylenimine impregnated protonated titanate nanotubes
topic computational fluid dynamic simulation
chemical reactions
MFiX
solid amine‐based carbon capture
titanate nanotubes
url https://doi.org/10.1002/ese3.665
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