Economic Analysis of Organic Rankine Cycle Using R123 and R245fa as Working Fluids and a Demonstration Project Report

被引:32
|
作者
Zhang, Xinxin [1 ,2 ]
Cao, Min [1 ,2 ]
Yang, Xiaoyu [1 ,2 ]
Guo, Hang [1 ,2 ]
Wang, Jingfu [1 ,2 ]
机构
[1] Beijing Univ Technol, Coll Environm & Energy Engn, Key Lab Enhanced Heat Transfer & Energy Conservat, Minist Educ, Beijing 100124, Peoples R China
[2] Beijing Univ Technol, Coll Environm & Energy Engn, Key Lab Heat Transfer & Energy Convers, Beijing 100124, Peoples R China
来源
APPLIED SCIENCES-BASEL | 2019年 / 9卷 / 02期
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
organic Rankine cycle; economic indicators; economic performance analysis; R123; R245fa; demonstration project; WASTE HEAT-RECOVERY; LOW-GRADE HEAT; TRANSCRITICAL POWER CYCLES; EXERGOECONOMIC ANALYSIS; THERMOECONOMIC OPTIMIZATION; PERFORMANCE EVALUATION; GENERAL CORRELATION; ORC; MIXTURES; SYSTEM;
D O I
10.3390/app9020288
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The organic Rankine cycle (ORC) is a popular technology used in waste heat recovery and low-grade heat utilization, which are two important measures to solve the problems brought by the energy crisis. The economic performance of ORC system is an important factor affecting its application and development. Therefore, the economic analysis of ORC is of great significance. In this study, R123 and R245fa, two frequently-used working fluids during the transition period, were selected for calculating and analyzing the economic performance of an ORC used for recovery of waste heat with a low flow rate and medium-low temperature. Five traditional economic indicators, namely total cost, net earnings, payback period, return on investment, levelized energy cost, and present value of total profit in system service life, which is a relatively new indicator, were used to establish the economic analysis model of ORC. The variation effects of evaporation temperature, condensation temperature of working fluid, flue gas inlet temperature, and mass flow rate of flue gas on the above six economic indicators were analyzed. The results show that the optimal evaporation temperature of R123 is 125 degrees C, the optimal condensation temperature is 33 degrees C, and the optimal heat source temperature is 217 degrees C. For R245fa, the optimal evaporation temperature is 122 degrees C, the optimal condensation temperature is 27 degrees C, and the optimal heat source temperature is 177 degrees C. The economic performance of an ORC demonstration project was reported and used for comparison with the estimation and analysis. It was found that the single screw expander has an excellent economy performance, which greatly reduces the proportion of expander cost in the ORC system.
引用
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页数:26
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