Modelling of heat exchangers based on thermochemical material for solar heat storage systems
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In: Energy Procedia, Vol. 61, 01.01.2014, p. 2809-2813.
Research output: Journal contributions › Conference article in journal › Research › peer-review
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TY - JOUR
T1 - Modelling of heat exchangers based on thermochemical material for solar heat storage systems
AU - Fopah Lele, Armand
AU - Rönnebeck, Thomas
AU - Rohde, Christian
AU - Schmidt, Thomas
AU - Kuznik, Frédéric
AU - Ruck, Wolfgang
N1 - Paper in the proceedings of the 6th ICAE in Taiwan, and published in Energy Procedia Journal 2014. Funding Information: This work was performed under research project innovation-inkubator / competence tandem “thermische batterie”. The authors would like to acknowledge the support of the EU-foerdert niedersachsen (EFRE), the Leuphana University of Lueneburg to have financed this project. Publisher Copyright: © 2014 The Authors.
PY - 2014/1/1
Y1 - 2014/1/1
N2 - In solar thermal energy storage systems the operation modes involve charging and discharging. This paper focuses only on the charging leading to an endothermic reaction and therefore an efficient heat exchanger is required to transfer the heat for fast and complete charging. Two different heat exchangers are studied in this paper. A plate fin and helical coil heat exchangers embedded in a magnesium chloride bed is modelled and solved using the software Comsol 4.3a based on finite element method. Meshing analysis is performed for parameters sensibility and the results show a temperature variation of 13 °C (helical coil) and 19 °C (plate fin) in the material bed during the charging mode of the thermochemical heat storage system. The pressure distribution in the heat transfer fluid and the temperature distribution in the material bed are presented and the calculated overall heat transfer coefficient of 173 W/m 2 K (helical coil) and 236 W/m 2 K (plate-fin) are obtained on the base of the total heat transferred (Q) to through the system. The fluid flow is in turbulence regime (Re = 13200) in the fin-plate, but in laminar mode (can be kept up to Re = 20000) [1] in the coil because the flow is affected by secondary flow cause by centrifugal forces. This study allows the choice of the h eat exchanger wherein with first experiment has been made and compared.
AB - In solar thermal energy storage systems the operation modes involve charging and discharging. This paper focuses only on the charging leading to an endothermic reaction and therefore an efficient heat exchanger is required to transfer the heat for fast and complete charging. Two different heat exchangers are studied in this paper. A plate fin and helical coil heat exchangers embedded in a magnesium chloride bed is modelled and solved using the software Comsol 4.3a based on finite element method. Meshing analysis is performed for parameters sensibility and the results show a temperature variation of 13 °C (helical coil) and 19 °C (plate fin) in the material bed during the charging mode of the thermochemical heat storage system. The pressure distribution in the heat transfer fluid and the temperature distribution in the material bed are presented and the calculated overall heat transfer coefficient of 173 W/m 2 K (helical coil) and 236 W/m 2 K (plate-fin) are obtained on the base of the total heat transferred (Q) to through the system. The fluid flow is in turbulence regime (Re = 13200) in the fin-plate, but in laminar mode (can be kept up to Re = 20000) [1] in the coil because the flow is affected by secondary flow cause by centrifugal forces. This study allows the choice of the h eat exchanger wherein with first experiment has been made and compared.
KW - Engineering
KW - Heat exchanger
KW - Thermal power
KW - Energy research
KW - Heat and mass transfer
KW - convection
KW - Chemistry
KW - Thermochemical materials
KW - thermal decomposition
UR - http://www.scopus.com/inward/record.url?scp=84922376352&partnerID=8YFLogxK
U2 - 10.1016/j.egypro.2014.12.284
DO - 10.1016/j.egypro.2014.12.284
M3 - Conference article in journal
VL - 61
SP - 2809
EP - 2813
JO - Energy Procedia
JF - Energy Procedia
SN - 1876-6102
ER -