A new carbon-negative hydrogen production cycle for better sustainability.

IF 8 2区 环境科学与生态学 Q1 ENVIRONMENTAL SCIENCES Journal of Environmental Management Pub Date : 2024-10-07 DOI:10.1016/j.jenvman.2024.122695
Mert Temiz, Ibrahim Dincer
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Abstract

Carbon dioxide removal is considered by many as an essential piece to achieve global net zero targets which was also mentioned by the third working group of Intergovernmental Panel on Climate Change. On top of this, green hydrogen is badly needed to achive carbon-free society long-term sustainability. This study proposes a new five-step sodium hydroxide thermochemical cycle for simultaneous hydrogen production and carbon dioxide removal, which is driven by the heat at least 400 °C. The proposed integrated cycle can be driven by clean energy sources that can be utilized to generate heat at required temperatures. The proposed system is designed and analyzed by using energy and exergy approaches of thermodynamics. A case study is also developed in order to understand the effects of changing parameters on system performance. A thermochemical hydrogen production cycle is designed with an unequilibrium reaction where the respective heat capacity calculation models are employed. According to the calculations, more than half of the energy content of process heat can be converted into hydrogen, where maximum energy and exergy efficiencies of the thermochemical cycle are found as 50.05% and 76.61% when the separation reaction is carried out at 400 °C. According to the case study results, a parabolic trough collector type concentrated solar energy system with 295 kW of heat sink capacity, can generate 5216.65 kg of hydrogen and capture 19,991.97 kg of carbon dioxide in a location where 1500.11 kWh of solar energy is reached per m2 of area in a typical year.

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新的负碳制氢循环可实现更好的可持续性。
许多人认为,清除二氧化碳是实现全球净零排放目标的重要一环,政府间气候变化专门委员会第三工作组也提到了这一点。此外,要实现无碳社会的长期可持续发展,迫切需要绿色氢气。本研究提出了一种新的五步氢氧化钠热化学循环,可同时制氢和去除二氧化碳,该循环由至少 400 °C 的热量驱动。拟议的综合循环可由清洁能源驱动,这些能源可用于产生所需温度的热量。该系统的设计和分析采用了热力学的能量和放能方法。此外,还进行了案例研究,以了解参数变化对系统性能的影响。设计了一个不平衡反应的热化学制氢循环,并采用了相应的热容量计算模型。根据计算结果,超过一半的工艺热能可转化为氢气,当分离反应在 400 °C 下进行时,热化学循环的最大能量效率和放能效率分别为 50.05% 和 76.61%。根据案例研究结果,抛物槽集热器式聚光太阳能系统的散热能力为 295 千瓦,在典型年份每平方米面积的太阳能消耗量为 1500.11 千瓦时的地点,该系统可产生 5216.65 千克氢气,并捕获 19991.97 千克二氧化碳。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Journal of Environmental Management
Journal of Environmental Management 环境科学-环境科学
CiteScore
13.70
自引率
5.70%
发文量
2477
审稿时长
84 days
期刊介绍: The Journal of Environmental Management is a journal for the publication of peer reviewed, original research for all aspects of management and the managed use of the environment, both natural and man-made.Critical review articles are also welcome; submission of these is strongly encouraged.
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