Coupled modeling of combustion and heat transfer process of a supercritical CO2 boiler

被引:9
|
作者
Yang, Yu [1 ]
Li, Hongzhi [1 ]
Zhang, Yifan [1 ]
Bai, Wengang [1 ]
Yao, Mingyu [1 ]
机构
[1] Xian Thermal Power Res Inst Co Ltd, Xian 710054, Peoples R China
基金
中国国家自然科学基金;
关键词
Supercritical CO2 boiler; Coupled heat transfer; Superheater; Re-heater; SIMULATION; HYDRODYNAMICS; CHAMBER; TUBE;
D O I
10.1016/j.fuel.2020.118294
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this paper, the heat transfer process of high temperature heating surfaces in a 20 MWth supercritical CO2 (SCO2) boiler is integrally modeled by combining the one dimensional (1D) analytical model for supercritical CO2 and the three dimensional (3D) CFD model for combustion and heat transfer process of flue gas. The 20 MWth SCO2 boiler is designed for a 5 MWe S-CO2 power generation platform being constructed by Xi'an Thermal Power Research Institute Co., Ltd. The numerical results indicate that the tube wall temperature of gas cooling wall increases gradually along the S-CO2 flow direction, and the maximum wall temperature appears at the outlet region of the Front wall where the temperature reaches 907 K. The maximum temperature of tube wall in superheater and re-heater is around 950 K. The heat flux and temperature distributions of tube walls in superheater and re-heater are extremely non-uniform, which makes the traditional design method not practical in designing S-CO2 serpentine heat exchangers. The integral modeling method put forward in this work has the ability to capture the non-uniform heat transfer process in superheater and re-heater, and hence it is an efficient tool to study the sophisticated phenomena in S-CO2 boiler.
引用
收藏
页数:12
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