通过氧化钴循环展示可持续、多年的太阳能热化学储能技术

Katherine Bassett, Rachel Silcox, Jeffrey D. Will, Sarah Hill, Paul Smith, Ben Smith, Brian Schmit, Luke J. Venstrom, Peter Krenzke
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摘要

我们展示了太阳能热化学储能的概念验证,时间跨度为多年。这种储能是可互换的,可以采用工艺热或氢的形式。我们设计并制造了一个 4 千瓦的太阳能转鼓反应器,通过金属氧化物还原-氧化循环执行太阳能热化学储能的太阳能驱动充电步骤。2019 年夏季,太阳能反应器在瓦尔帕莱索大学的太阳能炉中运行,在约 1000°C 的温度下实现亚毫米氧化钴颗粒在空气中的还原。颗粒收集系统对还原颗粒进行了快速冷却,使其在进料速率为 2.9-60.8 克/分钟-1 时的转化率保持在 84-94% 之间。太阳能-化学储存效率(定义为 1000°C 下还原反应的焓除以输入的太阳能)达到 20%。还原氧化钴颗粒样品在室温空气中储存在小瓶中超过三年。通过在台式反应器中对空气中的样品进行再氧化,以及对样品进行电化学再氧化以产生 H2,来释放所储存的太阳能。通过测量还原金属氧化物对氧气的吸收,证实了它有望成为一种长时间储存和释放太阳能的介质。线性扫频伏安法和大容量电解法证明,相对于普通氢电极,在 0.55 V 的电压下就能产生 H2,比传统电解所需的 1.23 V 电位低 0.68 V。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Fungible, Multiyear Solar Thermochemical Energy Storage Demonstrated via the Cobalt Oxide Cycle
We present a proof of concept demonstration of solar thermochemical energy storage on a multiple year time scale. The storage is fungible, and can take the form of process heat or hydrogen. We designed and fabricated a 4-kW solar rotary drum reactor to carry out the solar-driven charging step of solar thermochemical storage via metal oxide reduction- oxidation cycles. During the summer of 2019, the solar reactor was operated in the Valparaiso University solar furnace to effect the reduction of submillimeter cobalt oxide particles in air at approximately 1000°C. A particle collection system cooled the reduced particles rapidly enough to maintain conversions of 84–94% for feed rates of 2.9–60.8 g min−1. The solar-to-chemical storage efficiency, defined as the enthalpy of the reduction reaction at 1000°C divided by the solar energy input, reached 20%. Samples of the reduced cobalt oxide particles were stored in vials in air at room temperature for more than three years. The stored solar energy was released by reoxidizing samples in air in a benchtop reactor and by electrochemically reoxidizing samples to produce H2. Measurements of the oxygen uptake by the reduced metal oxide confirm its promise as a medium to store and dispatch solar energy over long durations. Linear sweep voltammetry and bulk electrolysis demonstrate the promise of H2 production at 0.55 V relative to the normal hydrogen electrode, 0.68 V below the 1.23 V potential required for conventional electrolysis.
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