{"title":"Revolutionizing 300 °C industrial steam with a novel transcritical carbon dioxide heat pump system: Thermodynamic and configuration analyses","authors":"Shaoqiang Li, Yulong Song, Tianliang Chang, Qingsheng Yu, Yuchen Zhang, Feng Cao","doi":"10.1016/j.enconman.2025.120556","DOIUrl":null,"url":null,"abstract":"<div><div>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.</div></div>","PeriodicalId":11664,"journal":{"name":"Energy Conversion and Management","volume":"346 ","pages":"Article 120556"},"PeriodicalIF":10.9000,"publicationDate":"2025-09-27","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Energy Conversion and Management","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0196890425010805","RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
Abstract
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.
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.