Thermodynamic and techno-economic analysis of a direct thermal oil vaporization solar power system

被引:2
作者
Li, Pengcheng [1 ,3 ]
Ye, Jing [1 ]
Li, Jing [2 ]
Wang, Yandong [4 ]
Jiang, Xiaobin [1 ]
Qian, Tongle [1 ]
Pei, Gang [5 ]
Liu, Xunfen [1 ]
机构
[1] Hefei Univ Technol, Sch Automot & Transportat Engn, 193 Tunxi Rd, Hefei, Peoples R China
[2] Univ Hull, Energy & Environm Inst, Res Ctr Sustainable Energy Technol, Kingston Upon Hull HU6 7RX, England
[3] DONGFANG Elect Dongfang Boiler Grp CO LTD, 150 Huangjue Ping, Wuxing St, Zigong, Peoples R China
[4] Hefei Gen Machinery Res Inst, 888 Changjiang Rd, Hefei, Peoples R China
[5] Univ Sci & Technol China, Dept Thermal Sci & Energy Engn, 96 Jinzhai Rd, Hefei, Peoples R China
基金
中国国家自然科学基金;
关键词
Solar thermal power generation; Subcritical steam rankine cycle; Thermal oil; Organic rankine cycle; Equivalent heat-to-power efficiency; ORGANIC RANKINE-CYCLE; ENERGY STORAGE; WORKING FLUIDS; WASTE HEAT; TEMPERATURE; PERFORMANCE; OPTIMIZATION; EFFICIENCY; DESIGN; DRIVEN;
D O I
10.1016/j.energy.2023.128963
中图分类号
O414.1 [热力学];
学科分类号
摘要
A unique direct thermal oil vaporization solar power system employing cascade organic-steam Rankine cycle is proposed. The oil is a mixture of biphenyl and diphenyl oxide, and it is used for heat transfer, storage and power cycle fluid in the novel system. Stable electricity output and prolonged storage capacity can be facilitated. In the rated mode, the oil is vaporized at 390 degrees C in the collectors and drives a top turbine. The exhaust heat is used for preheating and evaporating water of the bottom cycle. Meanwhile, the hot oil in a high-temperature tank (HTT) superheats and reheats the generated steam. When the irradiation is insufficient, the heat released by the oil from the HTT to a low-temperature tank drives the bottom cycle. Fundamentals, thermodynamic performance and techno-economic feasibility are elaborated. The results indicate that, compared with the mainstream dual-tank solar power systems, the proposed system has a higher thermal efficiency with a lower water evaporation temperature (42.90% at 260 degrees C vs. 38.06% at 310 degrees C) and a larger temperature drop between the two tanks (121 degrees C vs. 100 degrees C). The equivalent payback time with respect to the top oil cycle is less than 3 years.
引用
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页数:15
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