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Integration of calcium looping and calcium hydroxide thermochemical systems for energy storage and power production in concentrating solar power plants
被引:18
|作者:
Carro, A.
[1
]
Chacartegui, R.
[1
,3
]
Ortiz, C.
[2
]
Arcenegui-Troya, J.
[4
]
Perez-Maqueda, L. A.
[4
]
Becerra, J. A.
[1
,3
]
机构:
[1] Univ Seville, Dept Ingn Energet, Camino Descubrimientos S-N, Seville 41092, Spain
[2] Univ Loyola Andalucia, Dept Engn, Mat & Sustainabil Grp, Avda Univ S-N, Dos Hermanas 41704, Seville, Spain
[3] Univ Seville, Lab Engn Energy & Environm Sustainabil, Seville 41092, Spain
[4] CSIC Univ Sevilla, Inst Ciencia Mat Sevilla, Americo Vespucio 49, Seville 41092, Spain
来源:
关键词:
Thermochemical energy storage;
CSP;
Calcium looping;
Calcium hydroxide;
Calcium oxide;
Calcium carbonate;
100-PERCENT RENEWABLE ENERGY;
HEAT-TRANSFER;
MULTICYCLE ACTIVITY;
CO2;
CAPTURE;
LAB SCALE;
GENERATION;
CAO/CA(OH)(2);
TEMPERATURE;
CA(OH)(2);
PRESSURES;
D O I:
10.1016/j.energy.2023.128388
中图分类号:
O414.1 [热力学];
学科分类号:
摘要:
Energy storage is a key factor in the development of renewables-based electrical power systems. In recent years, the thermochemical energy storage system based on calcium-looping has emerged as an alternative to molten salts for energy storage in high-temperature concentrated solar power plants. This technology still presents some challenges that could be solved by integrating the thermochemical energy storage system based on calcium hydroxide. This work studies a novel concentrated solar power system integrating calcium-looping and calcium hydroxide thermochemical energy storage systems. The results show that the combined use of hydration -dehydration cycles in the calcination-carbonation processes of the calcium looping for energy storage could partially solve the issue related to the multicyclic deactivation of calcium oxide. The improvement in the con-version of calcium oxide during carbonation is demonstrated experimentally when hydration-dehydration cycles are combined. Numerical simulations demonstrate the technical feasibility of the integrated process, with effi-ciencies ranging between 38-46%, improved with the increase in calcium oxide conversion in the carbonator, showing the potential of the proposed integration.
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页数:17
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