Synthesis and simultaneous optimization of multi-heat source multi-pressure evaporation organic Rankine cycle with mixed working fluid

被引:18
|
作者
Liang, Zheng [1 ]
Liang, Yingzong [1 ,2 ]
Luo, Xianglong [1 ,2 ]
Chen, Jianyong [1 ,2 ]
Yang, Zhi [1 ,2 ]
Wang, Chao [1 ,2 ]
Chen, Ying [1 ,2 ]
机构
[1] Guangdong Univ Technol, Sch Mat & Energy, Guangzhou, Peoples R China
[2] Guangdong Univ Technol, Guangdong Prov Key Lab Funct Soft Matter, Guangzhou, Peoples R China
基金
中国国家自然科学基金;
关键词
Organic Rankine cycle; Mixed working fluid; Multi-pressure evaporation; Heat integration; Multi-heat source; LIQUID SEPARATION CONDENSER; LOW-GRADE HEAT; WASTE HEAT; ZEOTROPIC MIXTURES; PARAMETRIC OPTIMIZATION; PERFORMANCE ANALYSIS; EXERGY ANALYSIS; ORC; DESIGN; PLANT;
D O I
10.1016/j.enconman.2021.114930
中图分类号
O414.1 [热力学];
学科分类号
摘要
The organic Rankine cycle (ORC)'s performance relies on heat source properties, cycle structures, and working fluids. Influences of these factors, however, are often interdependent, making it difficult to determine the optimal design of ORC systems. To address this issue, we propose a mixed-integer nonlinear programming model for the multi-pressure evaporation ORCs driven by multiple heat sources that not only optimizes operating conditions, but also identifies the best working fluid composition and cycle structure. Results demonstrate that the proposed model is accurate and effective. The dual-pressure evaporation ORC driven by multi-heat source shows a 10.87% rise in the net power output (NPO) compared to the one with single pressure evaporation. In general, 0.9/0.1 npentane/n-heptane is the optimal mixed working fluid generating 2.71-12.11% more power than the pure working fluids for the numerical studies. Dual-pressure evaporation ORC is found to be a balanced design for the multi-heat source driven ORC in terms of its NPO and cycle complexity.
引用
收藏
页数:18
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