Author
Listed:
- Yuxuan Ji
(State Key Laboratory of Clean Energy Utilization, Zhejiang University, 38 Zheda Road, Hangzhou 310027, China)
- Zheng Wang
(State Key Laboratory of Clean Energy Utilization, Zhejiang University, 38 Zheda Road, Hangzhou 310027, China)
- Mingxuan Wang
(State Key Laboratory of Clean Energy Utilization, Zhejiang University, 38 Zheda Road, Hangzhou 310027, China)
- Yafei Liu
(State Key Laboratory of Clean Energy Utilization, Zhejiang University, 38 Zheda Road, Hangzhou 310027, China)
- Haoran Xu
(State Key Laboratory of Clean Energy Utilization, Zhejiang University, 38 Zheda Road, Hangzhou 310027, China)
- Peiwang Zhu
(State Key Laboratory of Clean Energy Utilization, Zhejiang University, 38 Zheda Road, Hangzhou 310027, China)
- Shilei Ma
(Shanghai Electric Power Generation Equipment Co., Ltd., 621 Longchang Road, Shanghai 200090, China)
- Zhigang Yang
(Shanghai Electric Power Generation Equipment Co., Ltd., 621 Longchang Road, Shanghai 200090, China)
- Gang Xiao
(State Key Laboratory of Clean Energy Utilization, Zhejiang University, 38 Zheda Road, Hangzhou 310027, China)
Abstract
The supercritical carbon dioxide (sCO 2 ) Brayton cycle is the preferred power cycle for future nuclear energy, fossil energy, solar energy, and other energy systems. As the preferred regenerator in the cycle, the printed circuit heat exchanger (PCHE) exhibits a high heat transfer efficiency, compactness, and robustness. The structure design of its internal flow channel is one of the most important factors to enhance the heat transfer and reduce pressure loss. In the present work, a trapezoidal PCHE prototype is designed and manufactured, and its thermal-hydraulic performance as a regenerator is experimentally studied in the sCO 2 test loop. The overall heat transfer coefficient exceeds 1.10 kW/(m 2 ·K) and reaches a maximum of 2.53 kW/(m 2 ·K) with the changes in the inlet temperature, the working pressure, and the mass flow rate. Correlations of the Nusselt numbers are proposed on both sides, with the Reynolds numbers ranging from 10,000 to 30,000 and 4800 to 14,000, and the Prandtl numbers ranging from 0.91 to 1.61 and 0.77 to 0.98 on the cold side and hot side, respectively. The pressure drop of the channels calculated by the peeling method using a single-plate straight prototype is less than 7 kPa and 15 kPa on the hot and the cold side, respectively. The heat recovery efficiency is analyzed to evaluate the performance as a regenerator. Finally, simulation works are carried out to verify the experimental results and expand the Reynolds numbers ranging from 3796 to 30,000 and 1821 to 14,000, on the cold side and hot side, respectively. This work provides the test methods and experimental correlations for the development of an efficient PCHE in the sCO 2 Brayton cycle.
Suggested Citation
Yuxuan Ji & Zheng Wang & Mingxuan Wang & Yafei Liu & Haoran Xu & Peiwang Zhu & Shilei Ma & Zhigang Yang & Gang Xiao, 2022.
"Experimental and Numerical Study on Thermal Hydraulic Performance of Trapezoidal Printed Circuit Heat Exchanger for Supercritical CO 2 Brayton Cycle,"
Energies, MDPI, vol. 15(14), pages 1-18, July.
Handle:
RePEc:gam:jeners:v:15:y:2022:i:14:p:4940-:d:856836
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Citations
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Cited by:
- George Stamatellos & Tassos Stamatelos, 2022.
"Effect of Actual Recuperators’ Effectiveness on the Attainable Efficiency of Supercritical CO 2 Brayton Cycles for Solar Thermal Power Plants,"
Energies, MDPI, vol. 15(20), pages 1-20, October.
- Haicai Lyu & Han Wang & Qincheng Bi & Fenglei Niu, 2022.
"Experimental Investigation on Heat Transfer and Pressure Drop of Supercritical Carbon Dioxide in a Mini Vertical Upward Flow,"
Energies, MDPI, vol. 15(17), pages 1-14, August.
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