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Hydrogen production by solar steam methane reforming with molten salts as energy carriers: Experimental and modelling analysis

机译:通过熔盐的太阳能蒸汽甲烷改造作为能量载体的氢气产生:实验和建模分析

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An innovative steam methane reforming for pure hydrogen production with molten salts as heat transfer fluid has been analyzed validating experimental data by means of a mathematical model. The technology, developed in the project CoMETHy and realized on a pilot scale at the ENEA-Casaccia research center, is based on a steam-reforming reactor with a structured open foam catalyst and Pd-based membranes, both integrated in the reaction environment to improve the reactor performance. The pilot plant allowed the production of = 3 Nm(3)/h of pure hydrogen, achieving an overall methane conversion of 60% at 545 degrees C reactor temperature. The mathematical model, composed of a partial differential equations set, has been solved by numerical simulation. The effects on pilot plant performance of some operating conditions, such as steam-to-carbon ratio, molten salt inlet temperature and sweep gas flow rate, have been investigated. The results obtained from model simulations have been compared to the available experimental data to validate the model. The average absolute error of the model is less than 2%. (c) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:通过数学模型分析了具有熔盐作为传热流体的纯氢生产的创新蒸汽甲烷重整。在项目中开发的技术,并在Enea-Casaccia研究中心的试验规模上实现,基于蒸汽重整反应器,其具有结构化开放的泡沫催化剂和基于Pd基膜,既集成在反应环境中以改善反应器性能。试验厂允许生产> = 3nm(3)/ h的纯氢,在<545℃反应器温度下实现60%的总甲烷转化。由数值模拟组成的数学模型通过数值模拟解决了。已经研究了对导液植物的影响,例如蒸汽与碳比,熔盐入口温度和扫描气流速率。从模型模拟获得的结果已与可用的实验数据进行比较以验证模型。模型的平均绝对误差小于2%。 (c)2020氢能源出版物LLC。 elsevier有限公司出版。保留所有权利。

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