Numerical investigation on heat transfer of supercritical CO2 in solar receiver tube in high temperature region

被引:1
作者
Zhuang Xiao-Ru [1 ]
Xu Xin-Hai [2 ]
Yang Zhi [3 ]
Zhao Yan-Xing [4 ]
Yu Peng [1 ]
机构
[1] Southern Univ Sci & Technol, Dept Mech & Aerosp Engn, Shenzhen 518055, Peoples R China
[2] Harbin Inst Technol Shenzhen, Sch Mech Engn & Automat, Shenzhen 518055, Peoples R China
[3] Guangdong Univ Technol, Sch Mat & Energy, Guangzhou 510006, Peoples R China
[4] Chinese Acad Sci, Tech Inst Phys & Chem, CAS Key Lab Cryogen, Beijing 100190, Peoples R China
基金
中国国家自然科学基金;
关键词
supercritical CO2; heat transfer; solar receiver tube; numerical simulation; CARBON-DIOXIDE; TRANSFER FLUID; BUOYANCY; FLOW; ACCELERATION;
D O I
10.7498/aps.70.20201005
中图分类号
O4 [物理学];
学科分类号
0702 ;
摘要
Supercritical CO2 can be used as a heat transfer fluid in a solar receiver, especially for a concentrating solar thermal power tower system. Such applications require better understanding of the heat transfer characteristics of supercritical CO2 in the solar receiver tube in a high temperature region. However, most of the existing experimental and numerical studies of the heat transfer characteristics of supercritical CO2 in tubes near the critical temperature region, and the corresponding heat transfer characteristics in the high temperature region are conducted. In this paper, a three-dimensional steady-state numerical simulation with the standard k-epsilon turbulent model is established by using ANSYS FLUENT for the flow and heat transfer of supercritical CO2 in a heated circular tube with an inner diameter of 6 mm and a length of 500 mm in the high temperature region. The effects of the fluid temperature (823-1023 K), the flow direction (horizontal, downward and upward), the pressure (7.5-9 MPa), the mass flux (200-500 kg.m(-2).s(-1)) and the heat flux (100-800 kW.m(-2)) on the convection heat transfer coefficient and Nusselt number are discussed. The results show that the convection heat transfer coefficient increases while Nusselt number decreases nearly linearly with fluid temperature increasing. Both fluid direction and pressure have negligible effects on the convection heat transfer coefficient and Nusselt number. Moreover, the convective heat transfer coefficient and Nusselt number are enhanced greatly with the increasing of mass flux and the decreasing of heat flux, which is more obvious at a higher heat flux. The influences of buoyancy and flow acceleration on the heat transfer characteristics are also investigated. The buoyancy effect can be ignored within the present parameter range. However, the flow acceleration induced by the high heat flux significantly deteriorates the heat transfer preformation. Moreover, eight heat transfer correlations of supercritical fluid in tubes are evaluated and compared with the present numerical data. The comparison indicates that the correlations based on the thermal property modification show better performance in the heat transfer prediction in the high temperature region than those based on the dimensionless number modification. And Nusselt number predicted by the best correlation has a mean absolute relative deviation of 8.1% compared with the present numerical results, with all predicted data points located in the deviation bandwidth of +/- 20%. The present work can provide a theoretical guidance for the optimal design and safe operation of concentrating solar receivers where supercritical CO2 is used as a heat transfer fluid.
引用
收藏
页数:13
相关论文
共 23 条
[1]  
[Anonymous], 1972, MATH MODELS TURBULEN
[2]   Review of heat transfer fluids in tube-receivers used in concentrating solar thermal systems: Properties and heat transfer coefficients [J].
Benoit, H. ;
Spreafico, L. ;
Gauthier, D. ;
Flamant, G. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2016, 55 :298-315
[3]  
Bishop A A, 1965, WCAP2056 WEST EL COR, P85
[4]   Numerical investigation of heat transfer in supercritical CO2 and water turbulent flow in circular tubes [J].
Bovard, Samaneh ;
Abdi, Mehdi ;
Nikou, Mohammad Reza Khosravi ;
Daryasafar, Amin .
JOURNAL OF SUPERCRITICAL FLUIDS, 2017, 119 :88-103
[5]   Supercritical CO2 as heat transfer fluid: A review [J].
Cabeza, Luisa F. ;
de Gracia, Alvaro ;
Ines Fernandez, A. ;
Farid, Mohammed M. .
APPLIED THERMAL ENGINEERING, 2017, 125 :799-810
[6]  
HALL WB, 1969, MECH ENG, V91, P66
[7]  
Huang X K, 2018, ACTA ENERGIAE SOLARI, V39, P44
[8]   Fluid flow and convective heat transfer to fluids at supercritical pressure [J].
Jackson, J. D. .
NUCLEAR ENGINEERING AND DESIGN, 2013, 264 :24-40
[9]   Experimental investigation of heat transfer in vertical upward and downward supercritical CO2 flow in a circular tube [J].
Kim, Dong Eok ;
Kim, Moo-Hwan .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2011, 32 (01) :176-191
[10]   Experimental study of the effects of flow acceleration and buoyancy on heat transfer in a supercritical fluid flow in a circular tube [J].
Kim, Dong Eok ;
Kim, Moo Hwan .
NUCLEAR ENGINEERING AND DESIGN, 2010, 240 (10) :3336-3349