Design and analysis of a nuclear and wind-based carbon negative potassium hydroxide water-splitting cycle for hydrogen and ammonia production

IF 3.9 2区 工程技术 Q2 COMPUTER SCIENCE, INTERDISCIPLINARY APPLICATIONS Computers & Chemical Engineering Pub Date : 2025-03-01 Epub Date: 2024-11-29 DOI:10.1016/j.compchemeng.2024.108964
Mert Temiz, Ibrahim Dincer
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Abstract

To achieve the net-zero target, clean energy sources, carbon-free fuels, and carbon capture are crucial pieces. The current study develops a new potassium hydroxide-based thermochemical water-splitting cycle and combines it with an ammonia export facility with community and data center. A sodium fast reactor and an offshore wind farm are considered to drive the integrated system to generate hydrogen, ammonia, electricity, heating and cooling. The proposed thermochemical water-splitting cycle uses 591 °C heat with a non-equilibrium reaction to generate hydrogen. The generated hydrogen is further used for ammonia generation via high-pressure ammonia reactor and pressure swing adsorption for nitrogen extraction from air. In the integration, sodium fast reactor provides the required heat to carry out integrated processes, where in high-temperature heat is distributed between the thermochemical cycle and the Rankine cycle, and the recovered heat is utilized in further processes. The proposed system is analyzed from thermodynamic aspects using energy and exergy approaches, supported by a parametric study. In addition, a time-dependent analysis is carried out under varying community and data center loads as well as varying wind speed, for each hour in a typical meteorological year. In the proposed integrated system, 230.4 MW of wind farm, 1 GWth of sodium fast reactor, a thermochemical cycle with 3.6 tonnes/hour hydrogen production and 78 tonnes/hour carbon capture capacities, a two-stage Rankine cycle, ammonia generator, and an absorption refrigeration cycle are considered. The energy and exergy efficiencies of newly developed five-step thermochemical cycle are 45.39 % and 62.78 % when reaction temperatures are considered as 240 °C for hydrogen generation and 591 °C for separation. For the integrated system, the overall energy and exergy efficiencies for the entire year are found as 32.61 % and 28.44 %.
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氢和氨生产的核能和风能负碳氢氧化钾水分解循环的设计和分析
为了实现净零目标,清洁能源、无碳燃料和碳捕获是至关重要的部分。目前的研究开发了一种新的基于氢氧化钾的热化学水分解循环,并将其与社区和数据中心的氨出口设施相结合。一个钠快堆和一个海上风电场被考虑驱动这个综合系统产生氢、氨、电、加热和冷却。提出的热化学水分解循环使用591°C的热量和非平衡反应产生氢。产生的氢气通过高压氨反应器和变压吸附从空气中提取氮气进一步用于制氨。在集成过程中,钠快堆提供所需的热量来进行集成过程,其中高温热量在热化学循环和朗肯循环之间分配,回收的热量用于进一步的工艺。从热力学角度出发,采用能量和火用方法对系统进行了分析,并进行了参数化研究。此外,在不同社区和数据中心负载以及不同风速的情况下,对典型气象年的每小时进行了时间相关分析。该综合系统考虑了230.4 MW风电场、1 GWth钠快堆、3.6吨/小时制氢和78吨/小时碳捕集能力的热化学循环、两级朗肯循环、氨发生器和吸收式制冷循环。当反应温度为240℃产氢和591℃分离时,新开发的五步热化学循环的能量效率和火用效率分别为45.39%和62.78%。对于集成系统,全年的总能源效率和火用效率分别为32.61%和28.44%。
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来源期刊
Computers & Chemical Engineering
Computers & Chemical Engineering 工程技术-工程:化工
CiteScore
8.70
自引率
14.00%
发文量
374
审稿时长
70 days
期刊介绍: Computers & Chemical Engineering is primarily a journal of record for new developments in the application of computing and systems technology to chemical engineering problems.
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