革命性的300°C工业蒸汽与一个新的跨临界二氧化碳热泵系统:热力学和配置分析

IF 10.9 1区 工程技术 Q1 ENERGY & FUELS
Shaoqiang Li, Yulong Song, Tianliang Chang, Qingsheng Yu, Yuchen Zhang, Feng Cao
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引用次数: 0

摘要

工业领域迫切需要高达300°c的高温蒸汽,这远远超出了传统热泵技术的能力。为了扩大高温热泵技术在工业蒸汽供应中的应用范围,本研究提出了一种新型的跨临界二氧化碳热泵,该热泵可以直接从环境空气中产生300℃的蒸汽作为热源。通过双气体冷却器配置将高压水加热和蒸汽过热物理分离,系统实现了蒸汽压力和温度的解耦控制。这种分阶段生成策略有效地利用了超临界二氧化碳的温度滑动来提供300°C的蒸汽,同时消除了低效的蒸汽再压缩的需要。建立了基于能量和火用分析的热力学模型来评价系统的性能。结果表明,与常规系统不同,该系统的性能系数和火用效率对排放压力相对不敏感。充分的内部热回收提高了性能系数和火用效率,同时创造了一个排放温度裕度,提供了在稳定的峰值性能下进一步提高蒸汽温度的灵活性。在热水出口温度为255°C时,峰值性能系数为1.65,最大火用效率为48.5%。配置比较表明,在较低的蒸汽压力下,双回热器配置比单回热器配置的效率优势主要是由于热交换器内的火用破坏显著减少。在较高的蒸汽压力下,单回热器配置在高排放压力下的性能系数最高,而双回热器配置更有利于在降低排放压力下保持较高的性能。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Revolutionizing 300 °C industrial steam with a novel transcritical carbon dioxide heat pump system: Thermodynamic and configuration analyses
The industrial fields have urgent demands for up to 300°C-grade high-temperature steam, which is far beyond the capability of conventional heat pump technologies. To expand the application range of high-temperature heat pump technology for industrial steam supply, this study proposes a novel transcritical carbon dioxide heat pump capable of directly generating 300 °C steam from ambient air as the heat source. By physically separating high-pressure water heating and steam superheating through a dual gas cooler configuration, the system achieves decoupled control of steam pressure and temperature. This staged generation strategy effectively exploits the temperature glide of supercritical carbon dioxide to supply 300 °C steam, while eliminating the need for inefficient steam recompression. The thermodynamic models based on energy and exergy analyses are developed to evaluate the system performance. The results indicate that the coefficient of performance and exergy efficiency are relatively insensitive to discharge pressure, which is different from conventional systems. Sufficient internal heat recovery enhances the coefficient of performance and exergy efficiency while creating a discharge temperature margin, providing the flexibility to further increase steam temperature at a stable peak performance. A peak coefficient of performance of 1.65 and a maximum exergy efficiency of 48.5 % are achieved at a heated water outlet temperature of 255 °C. A configuration comparison reveals that the efficiency advantage of the dual-recuperator configuration over the single-recuperator configuration at lower steam pressures is primarily due to the significant reduction in exergy destruction within the heat exchangers. At higher steam pressures, while the single-recuperator configuration achieves the highest coefficient of performance under high discharge pressures, the dual-recuperator configuration is more advantageous for maintaining higher performance at reduced discharge pressures.
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来源期刊
Energy Conversion and Management
Energy Conversion and Management 工程技术-力学
CiteScore
19.00
自引率
11.50%
发文量
1304
审稿时长
17 days
期刊介绍: The journal Energy Conversion and Management provides a forum for publishing original contributions and comprehensive technical review articles of interdisciplinary and original research on all important energy topics. The topics considered include energy generation, utilization, conversion, storage, transmission, conservation, management and sustainability. These topics typically involve various types of energy such as mechanical, thermal, nuclear, chemical, electromagnetic, magnetic and electric. These energy types cover all known energy resources, including renewable resources (e.g., solar, bio, hydro, wind, geothermal and ocean energy), fossil fuels and nuclear resources.
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