Thermoeconomic comparison between pure and mixture working fluids of organic Rankine cycles (ORCs) for low temperature waste heat recovery
文献类型：期刊论文
| 作者 | Feng, Yongqiang1; Hung, TzuChen2; Greg, Kowalski3; Zhang, Yaning1; Li, Bingxi1; Yang, Jinfu4 |
| 刊名 | ENERGY CONVERSION AND MANAGEMENT
 |
| 出版日期 | 2015-12-01 |
| 卷号 | 106页码:859-872 |
| 关键词 | Organic Rankine cycle (ORC) Thermoeconomic multi-objective optimization Exergy efficiency Levelized energy cost (LEC) Mixture working fluids |
| 英文摘要 | Based on the thermoeconomic multi-objective optimization, simultaneously considering exergy efficiency and levelized energy cost (LEC), the thermoeconomic comparisons between pure and mixture working fluids of organic Rankine cycles (ORCs) have been investigated. Four models are proposed based on the different location of evaporating bubble point temperature or condensing dew point temperature for mixture working fluids. The effects of mass fraction and four key parameters (evaporator temperature, condenser temperature, pinch point temperature difference and degree of superheat) on exergy efficiency and levelized energy cost (LEC) are examined. Pareto-optimal solutions of four models using 0.7R245fa/0.3R227ea are obtained and compared. Taking mass fraction into account, the thermoeconomic comparisons between pure and mixture working fluids have been studied. Research demonstrates that the mixtures don't always present better thermodynamic performance and economic performance than pure working fluids. Model 2 (T-7 = T-E, T-3 = T-C) is the favorable operation condition for its highest thermodynamic performance and relatively low economic factor. Taking mass fraction as decision variable, Pareto-optimal solutions for models 1, 2,3 and 4 in pairs of (exergy efficiency (%), LEC ($/kW h)) are (56.71, 0.188), (57.67, 0.192), (57.11, 0.194), and (56.91, 0.192), respectively. Compared with pure working fluids, the mixture working fluids present better exergy efficiency but worse LEC except model 1. (C) 2015 Elsevier Ltd. All rights reserved. |
| WOS标题词 | Science & Technology ; Physical Sciences ; Technology |
| 类目[WOS] | Thermodynamics ; Energy & Fuels ; Mechanics ; Physics, Nuclear |
| 研究领域[WOS] | Thermodynamics ; Energy & Fuels ; Mechanics ; Physics |
| 关键词[WOS] | LOW-GRADE HEAT ; ZEOTROPIC MIXTURES ; THERMODYNAMIC ANALYSIS ; POWER-GENERATION ; EXERGY ANALYSIS ; MULTIOBJECTIVE OPTIMIZATION ; PERFORMANCE ANALYSIS ; THERMAL EFFICIENCY ; KALINA CYCLE ; GAS-TURBINE |
| 收录类别 | SCI |
| 语种 | 英语 |
| WOS记录号 | WOS:000366063500078 |
| 公开日期 | 2016-03-15 |
| 源URL | [http://ir.etp.ac.cn/handle/311046/112314]  |
| 专题 | 工程热物理研究所_中国科学院工程热物理所（论文库）_期刊论文（SCI） |
| 作者单位 | 1.Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Peoples R China 2.Natl Taipei Univ Technol, Dept Mech Engn, Taipei, Taiwan 3.Northeastern Univ, Mech & Ind Engn, Boston, MA 02115 USA 4.Chinese Acad Sci, Inst Engn Thermophys, Beijing, Peoples R China |
| 推荐引用方式 GB/T 7714 | Feng, Yongqiang,Hung, TzuChen,Greg, Kowalski,et al. Thermoeconomic comparison between pure and mixture working fluids of organic Rankine cycles (ORCs) for low temperature waste heat recovery[J]. ENERGY CONVERSION AND MANAGEMENT,2015,106:859-872. |
| APA | Feng, Yongqiang,Hung, TzuChen,Greg, Kowalski,Zhang, Yaning,Li, Bingxi,&Yang, Jinfu.(2015).Thermoeconomic comparison between pure and mixture working fluids of organic Rankine cycles (ORCs) for low temperature waste heat recovery.ENERGY CONVERSION AND MANAGEMENT,106,859-872. |
| MLA | Feng, Yongqiang,et al."Thermoeconomic comparison between pure and mixture working fluids of organic Rankine cycles (ORCs) for low temperature waste heat recovery".ENERGY CONVERSION AND MANAGEMENT 106(2015):859-872. |
入库方式： OAI收割
来源：工程热物理研究所
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