The active design of mixtures based on transition temperature of heat source for organic Rankine cycle

被引:1
|
作者
Chen, Guibing [1 ]
An, Qingsong [1 ]
Zhao, Jun [1 ]
Chang, Nini [1 ]
Wang, Yongzhen [1 ]
Yin, Hongmei [1 ]
Hu, Likai [1 ]
Gong, Yulie [2 ]
Li, Xiaowei [3 ]
机构
[1] Tianjin Univ, MOE, Key Lab Efficient Utilizat Low & Medium Grade Ene, Tianjin 300350, Peoples R China
[2] Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China
[3] China Ship Dev & Design Ctr, Wuhan 430064, Hubei, Peoples R China
基金
中国国家自然科学基金;
关键词
Organic Rankine Cycle(ORC); Reverse design; Transition temperature of heat source temperature; Optimal evaporating temperature(OET); Critical temperature; WORKING FLUID SELECTION; EXERGY ANALYSIS;
D O I
10.1016/j.egypro.2019.01.402
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
This paper presents a theoretical EEM (exergy efficiency model) to study active design of mixtures based on the transition temperature of heat source for subcritical ORC (organic Rankine cycle). 15 working fluids with critical temperature from 100 degrees C to 200 degrees C are under evaluation. The exergy efficiency can be calculated quickly by the latent heat, specific heat at constant pressure and critical temperature based on the EEM. The maximal exergy efficiency will be obtained when the critical temperature of working fluid approaches to the heat source temperature. From the angle of reverse design, the ratios of mixtures can be calculated, whose exergy efficiency is higher than pure working fluids. Under the transition temperature, the exergy efficiency exists the maximum value with the OET. The increase of the OET is monotonous but not linear as the heat source temperature goes up. (C) 2019 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:1730 / 1736
页数:7
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