4.8 Article

Thermochemical reduction modeling in a high-temperature moving-bed reactor for energy storage: 1D model

期刊

APPLIED ENERGY
卷 306, 期 -, 页码 -

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.apenergy.2021.118009

关键词

Thermochemical energy storage; Moving-bed reactor; High-temperature; Thermal reduction; Heat transfer

资金

  1. U.S. Department of Energy's Office of Energy Efficiency and Renewable Energy (EERE) under the Solar Energy Technologies Office (SETO) [DE-EE0008992]

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Efficient high-temperature thermochemical reactors along with optimal operating conditions are crucial for achieving high-efficiency long-term solar energy storage. Computational modeling, coupled with experimental validation, is utilized to investigate the thermal reduction of metal oxide materials and enhance energy conversion efficiency in thermal reactors.
The design of robust and efficient high-temperature thermochemical reactors and determination of operating conditions are critical steps toward enabling high-efficiency long-duration solar energy storage. This work presents a computational model for the thermal reduction of a metal oxide material (Mg-Mn-O) up to 1450 degrees C and the coupled complex transport phenomena in a novel tubular thermal reactor design that features the capability for a high extent-of-reduction (high energy storage density) and inherent heat recuperation. A onedimensional model coupling counter-current gas-solid flow, two-phase heat transfer, thermochemical redox reactions, and species transport in a moving-bed reactor is developed. Simplified versions of the model are validated with published results in the literature for packed beds with both inert and reactive particles; the fully coupled model is also validated with experimental measurements of a moving-bed reactor in terms of local temperatures and oxygen release at the exit. Detailed comparisons on the effects of different boundary conditions in the reaction zone (prescribed wall temperature vs. heat flux conditions) and formulations based on a simple uniform flow assumption vs. plug flow using Ergun equation for gas flow are investigated. The results are compared with experimental measurements, and for all cases, the energy flow components in the reactor system and the thermal to chemical conversion efficiency and overall system efficiency are computed. The predicted high thermal-to-chemical efficiency -95% and system efficiency -30% agree with experimental measurements.

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