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High Temperature Thermochemical Heat Storage For Concentrated Solar Power Using Gas-Solid Reactions

机译:气固反应用于太阳能集中的高温热化学蓄热

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摘要

High temperature thermal storage technologies that can be easily integrated into future concentrated solar power plants are a key factor for increasing the market potential of solar power production. Storing thermal energy by reversible gas-solid reactions has the potential of achieving high storage densities while being adjustable to various plant configurations. In this paper the Ca{OH)ilCaO reaction system is investigated theoretically. It can achieve storage densities above 300 kWh/m3 while operating in a temperature range between 400 and 600°C. Reactor concepts with indirect and direct heat transfer are being evaluated. The low thermal conductivity of the fixed bed of solid reactants turned out to considerably limit the performance of a storage tank with indirect heat input through the reactor walls. A one-dimensional model for the storage reactor is established and solved with the Finite Element Method. The reactor concept with direct heat transfer by flowing the gaseous reactant plus additional inert gas through the solid reactants did not show any limitation due to heat transfer. If reaction kinetics are fast enough, the reactor performance in case of the CaiOHfolCaO reaction system is limited by the thermal capacity of the gaseous stream to take-up heat of reaction. However, to limit pressure drop and the according losses for compression of the gas stream, the size of the storage system is restricted in a fixed bed configuration.
机译:可以轻松集成到未来的集中式太阳能发电厂中的高温蓄热技术是增加太阳能发电市场潜力的关键因素。通过可逆的气固反应存储热能具有实现高存储密度的潜力,同时可以根据各种工厂配置进行调整。本文从理论上研究了Ca(OH)ilCaO反应体系。在400至600°C的温度范围内工作时,它可以实现300 kWh / m3以上的存储密度。具有间接和直接传热的反应堆概念正在评估中。事实证明,固体反应物固定床的低导热性极大地限制了通过反应器壁间接输入热量的储罐的性能。建立了存储反应器的一维模型,并用有限元法求解。通过使气态反应物和另外的惰性气体流过固体反应物而具有直接传热的反应器概念由于传热没有显示任何限制。如果反应动力学足够快,则在CaiOHfolCaO反应系统的情况下,反应器性能受到气流吸收反应热的热容量的限制。然而,为了限制压降和用于压缩气流的相应损失,在固定床构造中限制了存储系统的尺寸。

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