4.7 Article

Fluid selection and advanced exergy analysis of dual-loop ORC using zeotropic mixture

期刊

APPLIED THERMAL ENGINEERING
卷 185, 期 -, 页码 -

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.applthermaleng.2020.116423

关键词

Dual-loop organic Rankine cycle; Zeotropic mixture; Multi-objective optimization; Advanced exergy analysis

资金

  1. National Natural Science Foundation of China [51975503]
  2. Natural Science Foundation of Hunan Province, China [2018JJ2399]

向作者/读者索取更多资源

The study focuses on the comprehensive performance of a dual-loop organic Rankine cycle (DORC) influenced by working fluid pairs and key components. By conducting multi-objective optimization, suitable fluid pairs were selected and advanced exergy analysis was performed to estimate the improvement potential of each component. The results show that optimal performance can be achieved with specific mass fractions of zeotropic mixtures in the system.
The comprehensive performance of a dual-loop organic Rankine cycle (DORC) is mainly influenced by working fluid pairs and key components. Based on multi-objective optimization, we conducted the working fluid selection and advanced exergy analysis for the DORC system driven by flue gas at 300 degrees C. The exergy efficiency, payback period (PBP), and annual CO2 emission reduction (AER) were selected as the objective functions. Operating parameters and mass fraction of mixtures were optimized by non-dominated sorting genetic algorithm-II (NSGAII). A suitable fluid pair for the DORC system was selected from 13 candidate fluid pairs. Then, the improvement potential of each component was estimated based on advanced exergy analysis. The results show that there is an optimal mass fraction for different zeotropic mixtures. When cyclohexane/cyclopentane (0.2/0.8) and butane/pentane (0.65/0.35) are used for the high-temperature (HT) loop and low-temperature (LT) loop respectively, the DORC system can achieve the best performance. Its exergy efficiency and AER increase by 14.7% and 19.1% respectively, while PBP only increases by 2.6%, compared with the fluid pair of cyclohexane-butane. There is 261.9 kW endogenous avoidable exergy destruction in the DORC system, accounting for 53.5% of the total exergy destruction. The HT turbine (HTT) is the first component that needs technical modifications, followed by the HT evaporator (HTE), intermediate heat exchanger (IHE), and LT turbine (LTT).

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