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
中国国家自然科学基金; 国家重点研发计划;
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
收藏
页数:26
相关论文
共 50 条
  • [1] Performance Analysis of Organic Rankine Cycle With Working Fluid of R245fa/DMF
    Zhang, Xue-Feng
    Wang, Zi-Xuan
    Wang, Li-Wei
    [J]. Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics, 2021, 42 (02): : 280 - 286
  • [2] Experimental comparison of R245fa and R245fa/R601a for organic Rankine cycle using scroll expander
    Li, Tailu
    Zhu, Jialing
    Fu, Wencheng
    Hu, Kaiyong
    [J]. INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2015, 39 (02) : 202 - 214
  • [3] Performance evaluation of a partially admitted axial turbine using R245fa, R123 and their mixtures as working fluid for small-scale organic Rankine cycle
    Sun, Hongchuang
    Qin, Jiang
    Yan, Peigang
    Huang, Hongyan
    Hung, Tzu-Chen
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2018, 171 : 925 - 935
  • [4] Economical evaluation and optimization of organic Rankine cycle with mixture working fluids using R245fa as flame retardant
    Xi, Huan
    Li, Ming-Jia
    He, Ya-Ling
    Zhang, Yu-Wen
    [J]. APPLIED THERMAL ENGINEERING, 2017, 113 : 1056 - 1070
  • [5] Parametric optimization of organic Rankine cycle with R245fa/R601a as working fluid
    Zhu J.
    Kang Z.
    An Q.
    Li T.
    [J]. Transactions of Tianjin University, 2015, 21 (1) : 69 - 75
  • [6] Comparison of the Utilization of 110 °C and 120 °C Heat Sources in a Geothermal Energy System Using Organic Rankine Cycle (ORC) with R245fa, R123, and Mixed-Ratio Fluids as Working Fluids
    Surindra, Mochamad Denny
    Caesarendra, Wahyu
    Prasetyo, Totok
    Mahlia, Teuku Meurah Indra
    Taufik
    [J]. PROCESSES, 2019, 7 (02):
  • [7] Investigation of low-GWP working fluids as substitutes for R245fa in organic Rankine cycle application
    Yang, Min-Hsiung
    Liu, Ming-Chuan
    Yeh, Rong-Hua
    [J]. HELIYON, 2024, 10 (14)
  • [8] Parametric Optimization of Organic Rankine Cycle with R245fa/R601a as Working Fluid
    朱家玲
    康振华
    安青松
    李太禄
    [J]. Transactions of Tianjin University, 2015, (01) : 69 - 75
  • [9] Parametric Optimization of Organic Rankine Cycle with R245fa/R601a as Working Fluid
    朱家玲
    康振华
    安青松
    李太禄
    [J]. Transactions of Tianjin University., 2015, 21 (01) - 75
  • [10] NUMERICAL ANALYSIS OF A SOLAR ORGANIC RANKINE CYCLE (ORC) UNIT WITH R245FA AS WORKING FLUID
    Bamgbopa, Musbaudeen O.
    Uzgoren, Eray
    [J]. PROCEEDINGS OF THE ASME 6TH INTERNATIONAL CONFERENCE ON ENERGY SUSTAINABILITY - 2012, PTS A AND B, 2012, : 195 - 202