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Título
Thermo-economic optimization of an adiabatic compressed air energy storage system including system dynamics
Autor(es)
Palabras clave
Thermo-mechanical energy storage
Adiabatic compressed air energy storage
Radial packed-bed systems
Dynamical integrated model
Multi-objective optimization
Thermo-economic objective functions
Fecha de publicación
2026
Editor
Elsevier
Citación
Pérez-Gallego, D., Gonzalez-Ayala, J., Medina, A., Anvari, S., Calderón-Vásquez, I., Cardemil, J. M., & Calvo Hernández, A. (2026). Thermo-economic optimization of an adiabatic compressed air energy storage system including system dynamics. Journal of Energy Storage, 153, 121114. https://doi.org/10.1016/j.est.2026.121114
Resumen
[EN]Adiabatic compressed air energy storage is a promising, in-development technology for storing renewable
energy, for instance, from wind parks or photovoltaic installations. This work presents a multi-objective
thermoeconomic optimization analysis. It is based on a dynamic model of the plant’s thermodynamic
performance, in which the dynamics of the thermal energy storage (packed-bed type) and the charge and
discharge processes of the air reservoir are solved in detail. A plant configuration, as determined from
previous work in our group, with a priori good round-trip efficiencies (around 0.76–0.78), is considered the
starting point. It encompasses two-stage compression and expansion trains, along with two radial packedbeds
(utilizing either sensible or phase-change materials) to capitalize on the cooling between compression
steps. In the developed optimization procedure, the levelized cost of storage (LCoS) and the total capital
expenditure (CAPEX) are taken as key performance indicators. The decision variables include, among others,
mass flows, thermal energy storage dimensions, maximum and minimum cavern pressures, and the symmetry
of the pressure ratios between compressors and turbines. The optimization procedure uses an NSGA-II genetic
algorithm. One of the main novelties of the work is that accurate dynamic simulations have been used to obtain
Pareto fronts. They are analyzed from different perspectives: the size, geometry, and materials of the packedbeds;
the type of compressor (axial or centrifugal); energetic factors such as input and output energy and power;
the maximum pressures in the cavern; and the mass flows in the charge and discharge processes. Values of
LCoS are calculated with precision using realistic input data, resulting in approximately 80 e/MWh for a plant
capable of storing 600 MWh (reference power of 200 MW for charge periods of 3 h) and electricity prices during
charge of 50 e/MWh. The specific parameters and configurations that lead to those LCoS levels are made
explicit. Furthermore, the influence of cavern costs, charging electricity prices, and idle time is analyzed in
detail.
URI
ISSN
2352-152X
DOI
10.1016/j.est.2026.121114
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