Christopher Hall, Falk Schulze-Küppers, Kai Bittner, Bernd Büddefeld, Nikolaos Margaritis, Jörg Wolters, Sonja Groß-Barsnick, Juan Pablo Rincon Duarte, Nicole Carina Neumann, Ghaleb Natour
{"title":"A Proof-of-Concept Membrane Module Concept for Solar Thermal Water Splitting Using Oxygen Transport Membranes","authors":"Christopher Hall, Falk Schulze-Küppers, Kai Bittner, Bernd Büddefeld, Nikolaos Margaritis, Jörg Wolters, Sonja Groß-Barsnick, Juan Pablo Rincon Duarte, Nicole Carina Neumann, Ghaleb Natour","doi":"10.1002/ente.202402191","DOIUrl":null,"url":null,"abstract":"<p>Solar thermal water splitting using oxygen transport membranes enables sustainable hydrogen production and can thus play a key role in the emerging hydrogen economy. Membrane reactors potentially reduce temperature required by shifting the concentration equilibrium, thereby increasing the efficiency of thermal water splitting. This work presents a scaled-up proof-of-concept (PoC) module design for solar thermal water splitting applications utilizing oxygen transport membranes in relevant environments. The PoC module is based on a flexible and scalable stack design with parallel-oriented, membrane-containing layers, which supports the scalability of the concept. Solar heat integration is optimized for direct irradiation by a High Flux Solar Simulator. Key outcomes include focal point adjustments and design modifications using an irradiated copper plate to mitigate hot spots. The PoC module's material concept prevents thermal stresses and ensures gas-tight sealing of the membranes at an operating temperature of 850 °C under reducing and corrosive atmospheres. Optimal flow rates for steam (30–213 mmol min<sup>−1</sup>) and methane (8–54 mmol min<sup>−1</sup>) are calculated for the PoC module, resulting in efficient hydrogen (7–51 mmol min<sup>−1</sup>) and syngas (22–156 mmol min<sup>−1</sup>) production, using a membrane area of 167 cm<sup>2</sup>, with H<sub>2</sub>O and CH<sub>4</sub> conversion rates of 25% and 95%, respectively.</p>","PeriodicalId":11573,"journal":{"name":"Energy technology","volume":"13 10","pages":""},"PeriodicalIF":3.6000,"publicationDate":"2025-06-22","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://onlinelibrary.wiley.com/doi/epdf/10.1002/ente.202402191","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Energy technology","FirstCategoryId":"5","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/ente.202402191","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
Abstract
Solar thermal water splitting using oxygen transport membranes enables sustainable hydrogen production and can thus play a key role in the emerging hydrogen economy. Membrane reactors potentially reduce temperature required by shifting the concentration equilibrium, thereby increasing the efficiency of thermal water splitting. This work presents a scaled-up proof-of-concept (PoC) module design for solar thermal water splitting applications utilizing oxygen transport membranes in relevant environments. The PoC module is based on a flexible and scalable stack design with parallel-oriented, membrane-containing layers, which supports the scalability of the concept. Solar heat integration is optimized for direct irradiation by a High Flux Solar Simulator. Key outcomes include focal point adjustments and design modifications using an irradiated copper plate to mitigate hot spots. The PoC module's material concept prevents thermal stresses and ensures gas-tight sealing of the membranes at an operating temperature of 850 °C under reducing and corrosive atmospheres. Optimal flow rates for steam (30–213 mmol min−1) and methane (8–54 mmol min−1) are calculated for the PoC module, resulting in efficient hydrogen (7–51 mmol min−1) and syngas (22–156 mmol min−1) production, using a membrane area of 167 cm2, with H2O and CH4 conversion rates of 25% and 95%, respectively.
利用氧气传输膜进行太阳能热水分解,可以实现可持续的氢气生产,因此可以在新兴的氢经济中发挥关键作用。膜反应器有可能通过改变浓度平衡来降低所需的温度,从而提高热水分解的效率。这项工作提出了一个大规模的概念验证(PoC)模块设计,用于在相关环境中利用氧气传输膜的太阳能热水分解应用。PoC模块基于灵活且可扩展的堆栈设计,具有面向并行的膜层,支持概念的可扩展性。利用高通量太阳模拟器对太阳热集成进行了优化。主要成果包括焦点调整和设计修改,使用辐照铜板来减轻热点。PoC模块的材料概念可以防止热应力,并确保膜在850°C的工作温度下在还原性和腐蚀性气氛下的气密性。PoC模块计算了蒸汽(30-213 mmol min - 1)和甲烷(8-54 mmol min - 1)的最佳流量,使用167 cm2的膜面积,产生有效的氢气(7-51 mmol min - 1)和合成气(22-156 mmol min - 1),水和甲烷的转化率分别为25%和95%。
期刊介绍:
Energy Technology provides a forum for researchers and engineers from all relevant disciplines concerned with the generation, conversion, storage, and distribution of energy.
This new journal shall publish articles covering all technical aspects of energy process engineering from different perspectives, e.g.,
new concepts of energy generation and conversion;
design, operation, control, and optimization of processes for energy generation (e.g., carbon capture) and conversion of energy carriers;
improvement of existing processes;
combination of single components to systems for energy generation;
design of systems for energy storage;
production processes of fuels, e.g., hydrogen, electricity, petroleum, biobased fuels;
concepts and design of devices for energy distribution.