Thermodynamic and exergoeconomic analysis of a combined cooling, desalination and power system for low-grade waste heat utilization

被引:3
|
作者
Zhou, Shihe [1 ,3 ]
Zhang, Kechong [1 ]
Li, Min [1 ]
Yang, Wenkuan [1 ]
Shen, Shengqiang [2 ,3 ]
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
[3] Dalian Univ Technol, Key Lab Liaoning Prov Desalinat, Dalian 116024, Liaoning, Peoples R China
基金
中国国家自然科学基金;
关键词
Low-grade waste heat; Trans-critical organic Rankine cycle; Humidification-dehumidification desalination; Vapor compression refrigeration; Exergoeconomic; HUMIDIFICATION-DEHUMIDIFICATION DESALINATION; ORGANIC RANKINE CYCLES; PERFORMANCE ANALYSIS; PARAMETRIC ANALYSIS; THERMOECONOMIC ANALYSIS; ZEOTROPIC MIXTURES; DIESEL-ENGINE; OPTIMIZATION; ORC; DRIVEN;
D O I
10.1016/j.tsep.2023.102079
中图分类号
O414.1 [热力学];
学科分类号
摘要
As a form of sustainable energy, low-grade waste heat has considerable amount to be recovered, but the energy utilization efficiency is still low. In this paper, a novel multi-generation system is proposed to utilize the lowgrade waste heat efficiently and meet the needs for cooling, freshwater and power simultaneously, by integrating vapor compression refrigeration (VCR), humidification and dehumidification (HDH) desalination with transcritical organic Rankine cycle (TORC). Thermodynamic and exergoeconomic performances of the multigeneration system with five working fluids are evaluated. Parametric studies are conducted to identify the key operating parameters. Results show that the highest exergy efficiency eta ex and the lowest average unit cost of products (AUCP) can be obtained by using R161, while the highest coefficient of performance (COPtot) belongs to R143a. The proportion of the vapor generator in the total exergy destruction is the largest, followed by the condenser. Higher net power output and freshwater production can be achieved by raising the vapor generation temperature and the ratio of mass flow rates of working fluid, and the corresponding eta ex and AUCP are also improved. There is an optimal pressure for the lowest AUCP and the highest net power output and eta ex. Performance comparison with systems from the literature is conducted as well.
引用
收藏
页数:21
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