共 50 条
Energy, exergy and exergoeconomic analysis of a combined cooling, desalination and power system
被引:61
|作者:
Zhou, Shihe
[1
]
Liu, Xinyu
[1
]
Bian, Yongning
[1
]
Shen, Shengqiang
[2
]
机构:
[1] Dalian Univ Technol, Sch Ocean Sci & Technol, Panjin 124221, Liaoning, Peoples R China
[2] Dalian Univ Technol, Sch Energy & Power Engn, Dalian 116024, Liaoning, Peoples R China
基金:
中国国家自然科学基金;
国家重点研发计划;
关键词:
Ocean thermal energy;
Multi-generation;
Organic Rankine cycle;
Multi-effect distillation;
Ejector refrigeration;
Exergoeconomic;
ORGANIC RANKINE-CYCLE;
MULTIOBJECTIVE OPTIMIZATION;
MULTIEFFECT DISTILLATION;
PERFORMANCE SIMULATION;
POLYGENERATION SYSTEM;
PARAMETRIC ANALYSIS;
ECONOMIC-ANALYSIS;
WASTE-HEAT;
DESIGN;
REFRIGERATION;
D O I:
10.1016/j.enconman.2020.113006
中图分类号:
O414.1 [热力学];
学科分类号:
摘要:
Ocean thermal energy has attracted much attention for its unique advantages. Multi-generation systems are emerging as an effective solution to further improve energy efficiency and economy of ocean thermal energy conversion (OTEC) system. In this paper, a novel hybrid OTEC system combing cooling, desalination and power (CCDP) is proposed facing the actual demands of remote islands at low latitudes. The cogeneration of cooling capacity, fresh water and power are achieved by the subsystems of ejector refrigeration cycle (ERC), multi-effect distillation (MED) desalination and organic Rankine cycle (ORC). A detailed mathematical model for the proposed system is developed based on the thermodynamics and exergoeconomics. The effects of key operating parameters on the system performances are investigated from the perspectives of energy, exergy and exergoeconomic. The results indicate that the highest primary energy saving ratio (PESR) and exergy efficiency of the proposed system are up to 33.72% and 29.33%, respectively. The main sources of exergy destruction are the MED unit, generator and ejector, accounting for about 80% of the total exergy destruction. The improvement of both thermodynamic and exergoeconomic performances can be achieved at a higher generation pressure and a larger distillate production. The rise of condensing pressure is conducive to cutting down the unit costs of products, but will result in lower exergy efficiency and PESR.
引用
收藏
页数:18
相关论文