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Multi-Tubular Reactor for Hydrogen Production: CFD Thermal Design and Experimental Testing ?

机译:制氢用多管反应器:CFD热设计和实验测试

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This study presents the Computational Fluid Dynamics (CFD) thermal design and experimental tests results for a multi-tubular solar reactor for hydrogen production based on the ferrite thermochemical cycle in a pilot plant in the Plataforma Solar de Almería (PSA). The methodology followed for the solar reactor design is described, as well as the experimental tests carried out during the testing campaign and characterization of the reactor. The CFD model developed for the thermal design of the solar reactor has been validated against the experimental measurements, with a temperature error ranging from 1% to around 10% depending on the location within the reactor. The thermal balance in the reactor (cavity and tubes) has been also solved by the CFD model, showing a 7.9% thermal efficiency of the reactor. CFD results also show the percentage of reacting media inside the tubes which achieve the required temperature for the endothermic reaction process, with 90% of the ferrite pellets inside the tubes above the required temperature of 900 °C. The multi-tubular solar reactor designed with aid of CFD modelling and simulations has been built and operated successfully.
机译:这项研究介绍了基于铝质太阳能实验工厂(PSA)中的铁氧体热化学循环的,用于生产氢气的多管太阳能反应堆的计算流体动力学(CFD)热设计和实验测试结果。描述了太阳能反应堆设计所遵循的方法,以及在测试活动和反应堆表征过程中进行的实验测试。针对太阳能反应堆热设计开发的CFD模型已针对实验测量进行了验证,根据反应堆内的位置,温度误差范围为1%至10%。 CFD模型也解决了反应堆中(腔体和管道)的热平衡问题,反应堆的热效率为7.9%。 CFD结果还显示达到吸热反应过程所需温度的管内反应介质的百分比,管内90%的铁氧体小球高于所需温度900°C。借助CFD建模和仿真设计的多管太阳能反应器已成功建成并运行。

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