Thermal synthesis of a thermochemical heat storage with heat exchanger optimization

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Thermal synthesis of a thermochemical heat storage with heat exchanger optimization. / Fopah Lele, Armand; Kuznik, Frédéric; Osterland, Thomas et al.

in: Applied Thermal Engineering, Jahrgang 101, 25.05.2016, S. 669-677.

Publikation: Beiträge in ZeitschriftenZeitschriftenaufsätzeForschungbegutachtet

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Fopah Lele A, Kuznik F, Osterland T, Ruck W. Thermal synthesis of a thermochemical heat storage with heat exchanger optimization. Applied Thermal Engineering. 2016 Mai 25;101:669-677. doi: 10.1016/j.applthermaleng.2015.12.103

Bibtex

@article{35bd86d9fefc40c79470ec34c35faaa4,
title = "Thermal synthesis of a thermochemical heat storage with heat exchanger optimization",
abstract = "Thermochemical materials, particularly salt hydrates, have a significant potential for use in thermal energy storage systems. When a salt hydrate is heated to a critical temperature, a chemical reaction is initiated to dissociate it into its anhydrous form and water vapour. The anhydrous salt stores the sensible energy that was supplied for dehydration, which can be later extracted by allowing cooler water or water vapour to flow through the salt, transforming the stored energy into higher sensible heat. This work presents a thermal synthesis modelling of a thermochemical heat storage based on the reactive porous bed of MgCl 22H 2O in a closed system. An analytical sharp front model is also developed to determine the required hydration time and the optimal bed size for such a system at prototype level. A sensitivity analysis helps to identify the optimal parameters that significantly affect the performance of the heat release process. Numerical heat and mass transfer through principal system components is studied using Comsol Multiphysics Software. Numerical results show good concordance with the experiment and reveal that to achieve quasi-complete hydration of the bed, mass flow rate should not be higher than 0.001 kġh -1 for a bed thickness between 4 and 5 cm, considering the present system configuration. In this closed system, inlet vapour pressure into the bed has no influence on the conversion process. Optimal porosity of around 0.76 is found based on the heat and mass transfer dilemma analysis. Optimal heat exchanger design is performed for mass transfer enhancement in the reactive bed. ",
keywords = "Chemistry, Thermal synthesis, Thermochemical storage, Sharp front model, MgCl2⋅2H2O, Heat exchanger, Modelling, Sustainability Science, Energy research",
author = "{Fopah Lele}, Armand and Fr{\'e}d{\'e}ric Kuznik and Thomas Osterland and Wolfgang Ruck",
year = "2016",
month = may,
day = "25",
doi = "10.1016/j.applthermaleng.2015.12.103",
language = "English",
volume = "101",
pages = "669--677",
journal = "Applied Thermal Engineering",
issn = "1359-4311",
publisher = "Pergamon Press",

}

RIS

TY - JOUR

T1 - Thermal synthesis of a thermochemical heat storage with heat exchanger optimization

AU - Fopah Lele, Armand

AU - Kuznik, Frédéric

AU - Osterland, Thomas

AU - Ruck, Wolfgang

PY - 2016/5/25

Y1 - 2016/5/25

N2 - Thermochemical materials, particularly salt hydrates, have a significant potential for use in thermal energy storage systems. When a salt hydrate is heated to a critical temperature, a chemical reaction is initiated to dissociate it into its anhydrous form and water vapour. The anhydrous salt stores the sensible energy that was supplied for dehydration, which can be later extracted by allowing cooler water or water vapour to flow through the salt, transforming the stored energy into higher sensible heat. This work presents a thermal synthesis modelling of a thermochemical heat storage based on the reactive porous bed of MgCl 22H 2O in a closed system. An analytical sharp front model is also developed to determine the required hydration time and the optimal bed size for such a system at prototype level. A sensitivity analysis helps to identify the optimal parameters that significantly affect the performance of the heat release process. Numerical heat and mass transfer through principal system components is studied using Comsol Multiphysics Software. Numerical results show good concordance with the experiment and reveal that to achieve quasi-complete hydration of the bed, mass flow rate should not be higher than 0.001 kġh -1 for a bed thickness between 4 and 5 cm, considering the present system configuration. In this closed system, inlet vapour pressure into the bed has no influence on the conversion process. Optimal porosity of around 0.76 is found based on the heat and mass transfer dilemma analysis. Optimal heat exchanger design is performed for mass transfer enhancement in the reactive bed.

AB - Thermochemical materials, particularly salt hydrates, have a significant potential for use in thermal energy storage systems. When a salt hydrate is heated to a critical temperature, a chemical reaction is initiated to dissociate it into its anhydrous form and water vapour. The anhydrous salt stores the sensible energy that was supplied for dehydration, which can be later extracted by allowing cooler water or water vapour to flow through the salt, transforming the stored energy into higher sensible heat. This work presents a thermal synthesis modelling of a thermochemical heat storage based on the reactive porous bed of MgCl 22H 2O in a closed system. An analytical sharp front model is also developed to determine the required hydration time and the optimal bed size for such a system at prototype level. A sensitivity analysis helps to identify the optimal parameters that significantly affect the performance of the heat release process. Numerical heat and mass transfer through principal system components is studied using Comsol Multiphysics Software. Numerical results show good concordance with the experiment and reveal that to achieve quasi-complete hydration of the bed, mass flow rate should not be higher than 0.001 kġh -1 for a bed thickness between 4 and 5 cm, considering the present system configuration. In this closed system, inlet vapour pressure into the bed has no influence on the conversion process. Optimal porosity of around 0.76 is found based on the heat and mass transfer dilemma analysis. Optimal heat exchanger design is performed for mass transfer enhancement in the reactive bed.

KW - Chemistry

KW - Thermal synthesis

KW - Thermochemical storage

KW - Sharp front model

KW - MgCl2⋅2H2O

KW - Heat exchanger

KW - Modelling

KW - Sustainability Science

KW - Energy research

UR - http://www.scopus.com/inward/record.url?scp=84969941503&partnerID=8YFLogxK

U2 - 10.1016/j.applthermaleng.2015.12.103

DO - 10.1016/j.applthermaleng.2015.12.103

M3 - Journal articles

VL - 101

SP - 669

EP - 677

JO - Applied Thermal Engineering

JF - Applied Thermal Engineering

SN - 1359-4311

ER -

DOI