Mechanism and experimental study of supercritical CO2-water coupled heat transfer
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Affiliation:

1.College of Energy Engineering, Ministry of Education, Xi’an University of Science and Technology, Xi’an 710054, P. R. China;2.Key Laboratory of Western Mine Exploitation and Hazard Prevention, Ministry of Education, Xi’an University of Science and Technology, Xi’an 710054, P. R. China

Clc Number:

TK172

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Supported by Fok Ying Tung Education Foundation Program (71076), Basic Research Project of Natural Science in Shaanxi Province (2019JLP09) and the Xinjiang Production and Construction Corps key areas of science and technology research program funded projects (2019AB001).

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    Abstract:

    Under the background of the “dual carbon” goals, exploring new pathways for industrial restructuring, reducing carbon emissions, improving energy efficiency, and developing new high-quality productivity for CO2 high-energy utilization has become a research focus. To determine the mechanism of CO2 phase-change-induced cracking and expand its engineering applications, this study investigates the safety and environmental advantages of CO2 based on its multiphase characteristics and energy-utilization potential. A numerical gas-water coupling model is established. Using CO2 at 25 ℃ as the research object, a simulation scheme is designed to examine different water temperatures as heat-carrying fluids, thereby revealing the CO2-water heat-transfer mechanism under hydrothermal-CO2 coupling. Furthermore, the heat and mass transfer characteristics of two-phase flow are analyzed by a CO2-water enhanced tube-type heat-exchanger test. The results show that as the hydrothermal-fluid temperature increases, the CO2 heating rate increases proportionally: for every 1 ℃ increase in water temperature, CO2 temperature increases by 0.9 ℃. The water-stream temperature gradually decreases as CO2 absorbs heat, and the dissipation temperature of the hydrothermal fluid is proportional to the CO2 absorption temperature. The heat-transfer coefficient of the hydrothermal fluid increases from 1 790 W/(m2·K) to 2 090 W/(m2·K) and continues to rise with higher initial water temperatures. The heat transfer coefficient of CO2 is positively correlated with that of the hydrothermal fluids. The CO2 phase-change heat-absorption temperature shows an exponential growth trend with increasing water temperature. The maximum internal CO2 pressure increases from 131 MPa to 199 MPa, undergoing sequential stages: thermal expansion of liquid CO2, thermal expansion of gaseous CO2, phase-change energization, and pressure stabilization. CO2 heat absorption is positively correlated with the initial water temperature, and the thermal power of the water-flow heat source increases with rising water temperature. The effectiveness of supercritical CO2-water convective heat transfer is verified through the establishment of correlation equations and experimental analysis. This research provides significance theoretical and engineering insights for energy-conversion applications under non-uniform heat-flow conditions, such as photothermal systems, boilers, and CO2 fracturing and storage.

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邓广哲,蔚斐,袁超.超临界CO2-水耦合传热机理及试验研究[J].重庆大学学报,2026,49(4):63~80

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  • Received:July 04,2024
  • Revised:
  • Adopted:
  • Online: April 21,2026
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