Thermodynamic and economic analyses of natural gas combined cycle power plants with and without the presence of organic Rankine cycle

被引:0
作者
Gu, Feng [1 ]
Zhu, Zhaowei [2 ]
Shi, Qianqian [3 ]
Li, Ruihua [4 ]
机构
[1] Jiangsu Vocat Coll Elect & Informat, Business Sch, Huaian, Jiangsu, Peoples R China
[2] Zhongnan Univ Econ & Law, Sch Accounting, Wuhan 430200, Hubei, Peoples R China
[3] Nanjing Wenjing East Rd Primary Sch, Nanjing, Peoples R China
[4] Xuchang Univ, Sch Elect & Mech Engn, Xuchang, Henan, Peoples R China
关键词
Natural gas combined cycle; organic Rankine cycle; thermo-economic analysis; power plant; CO2; CAPTURE; OPTIMIZATION; SOLAR; NGCC; INTEGRATION; RECOVERY; EXERGY; ENERGY; ORCS; COAL;
D O I
10.1177/01445987231183178
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This study performs the simulation and energy, exergy, and economic analyses of an organic Rankine cycle (ORC) integrated with a natural gas combined cycle. Working fluids studied in this research are ammonia, isobutane, R-11, R-113, and R-141b. The power plant and ORC are simulated using Aspen HYSYS software. The results show that using the ORC leads to an improvement in the thermo-economic indexes of the combined cycle power plant. The sensitivity analysis also demonstrated that using ammonia and isobutane as working fluids results in the highest exergy destruction and the lowest exergy and energy efficiencies; therefore, they are unsuitable. On the other hand, a comparison of thermo-economic results illustrated that among the studied working fluids, R-113 is the desirable selection. According to the simulation, it is deduced that employing R-113 working fluid leads to the net power generation of the plant increasing by 2.48%, the cost of electricity decreasing by 10.75%, and the total energy efficiency of the power plant increasing by 6.02%.
引用
收藏
页码:1956 / 1982
页数:27
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