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Study on heat transfer performance of heat exchange tubes of supercritical carbon dioxide boilers
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Shengpeng WANG1, 2, Yu YANG2, Yike NI2, Jiarong WU2, Yongqiang QIAO2, Yifan ZHANG2, Hongzhi LI1, 2, Junjie YAN1
Thermal Power Generation | 2025, 54(4) : 95 - 103
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Thermal Power Generation | 2025, 54(4): 95-103
Special topic on new energy power generation technology
Study on heat transfer performance of heat exchange tubes of supercritical carbon dioxide boilers
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Shengpeng WANG1, 2, Yu YANG2, Yike NI2, Jiarong WU2, Yongqiang QIAO2, Yifan ZHANG2, Hongzhi LI1, 2, Junjie YAN1
Affiliations
  • 1.School of Energy and Power Engineering, Xi’an Jiaotong University, Xi’an 710049, China
  • 2.Xi’an Thermal Engineering Research Institute Co., Ltd., Xi’an 710054, China
Published: 2025-04-25 doi: 10.19666/j.rlfd.202409210
Outline
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Supercritical carbon dioxide (S-CO2) power generation technology offers better flexibility, and its substitution for steam power generation technology in the field of thermal power generation is of significant strategic importance for constructing a new type of power system, establishing a modern energy system, and achieving the “dual carbon” goal. Through numerical simulation and experiment, the flow and heat transfer characteristics of S-CO2 boilers within the actual operating range are analyzed, and the influence of working fluid flow states and physical properties on heat transfer and resistance performance is also investigated. The results show that, the heat transfer coefficient of CO2 decreases with the thermal conductivity under the same flow conditions. This is because the thermal resistance of the fluid boundary layer increases as the thermal conductivity decreases. Under the same thermal conductivity conditions, the heat transfer coefficient of CO2 increases with the Reynolds number (Re). The reason is that the fluid boundary layer becomes thinner as Re increases, reducing the boundary layer thermal resistance. For CO2 working fluid inside the pipe with pressures ranging from 3 MPa to 30 MPa, enthalpy values of 500~1 150 kJ/kg, and Re between 1.1×105 and 2.1×106, a correlation formula for heat transfer considering boundary layer property corrections is derived. The average deviations are 3.33%, demonstrating it has high precision. The research lays a solid foundation for the design and research of subsequent S-CO2 boilers.

supercritical carbon dioxide boiler  /  heat transfer  /  experiment measurement  /  numerical simulation
Shengpeng WANG, Yu YANG, Yike NI, Jiarong WU, Yongqiang QIAO, Yifan ZHANG, Hongzhi LI, Junjie YAN. Study on heat transfer performance of heat exchange tubes of supercritical carbon dioxide boilers[J]. Thermal Power Generation, 2025 , 54 (4) : 95 -103 . DOI: 10.19666/j.rlfd.202409210
  • Innovation Capability Support Program of Shaanxi(2023-CX-TD-18)
Year 2025 volume 54 Issue 4
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Article Info
doi: 10.19666/j.rlfd.202409210
  • Receive Date:2024-09-05
  • Online Date:2026-03-06
  • Published:2025-04-25
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History
  • Received:2024-09-05
Funding
Innovation Capability Support Program of Shaanxi(2023-CX-TD-18)
Affiliations
    1.School of Energy and Power Engineering, Xi’an Jiaotong University, Xi’an 710049, China
    2.Xi’an Thermal Engineering Research Institute Co., Ltd., Xi’an 710054, China
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表12种不同金属材料的力学参数

Family
属数
Number of
genus
种数
Number of
species
占总种数比例
Percentage of
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Genus
种数
Number of
species
占总种数比例
Percentage of total
species (%)
鹅膏菌科Amanitaceae 2 11 5.26 鹅膏菌属 Amanita 10 4.78
小菇科 Mycenaceae 2 12 5.74 丝盖伞属 Inocybe 5 2.39
多孔菌科 Polyporaceae 8 14 6.70 蜡蘑属 Laccaria 5 2.39
红菇科 Russulaceae 3 23 11.00 小皮伞属 Marasmius 6 2.87
小菇属 Mycena 11 5.26
光柄菇属 Pluteus 5 2.39
红菇属 Russula 17 8.13
栓菌属 Trametes 5 2.39
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