Exergy analysis of a coupled transcritical and subcritical organic Rankine cycle system for waste heat recovery

被引:3
|
作者
Gong, Xi-Wu [1 ]
Wang, Xiao-Qiong [2 ]
Li, You-Rong [2 ]
机构
[1] Zhejiang Ocean Univ, Sch Naval Architecture & Ocean Engn, Zhoushan 316022, Peoples R China
[2] Chongqing Univ, Coll Power Engn, Minist Educ, Key Lab Low Grade Energy Utilisat Technol & Syst, Chongqing 400044, Peoples R China
关键词
coupled organic Rankine cycle; CORC; exergy analysis; exergy efficiency; working fluid combination; WORKING FLUID SELECTION; CARBON-DIOXIDE; POWER; TEMPERATURE; OPTIMIZATION; ENERGY; ORC;
D O I
10.1504/IJEX.2016.077431
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper presents a detailed exergy analysis for a novel coupled organic Rankine cycle (CORC) system driven by the waste heat of the flue gas, which combined a transcritical organic Rankine cycle (TORC) with a subcritical organic Rankine cycle (SORC). The results show that the exergy efficiency of the CORC increases with the increase of the inlet pressure of the TORC expander and the decrease of the pinch point temperature difference of the internal heat exchanger. However, the increase of the flue gas temperatures at the inlet and outlet of the evaporator has negative effects. The CORC using isentropic working fluids exhibits better performance than that using dry working fluids. Furthermore, high critical temperature of the working fluid can improve the exergy efficiency. The exergy loss is mainly distributed in the heat exchangers and the expanders, which is different from the result in the traditional TORC.
引用
收藏
页码:361 / 380
页数:20
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