Dinitrogen tetroxide and carbon dioxide mixtures as working fluids in solar tower plants

被引:36
作者
Binotti, Marco [1 ]
Invernizzi, Costante M. [2 ]
Iora, Paolo [2 ]
Manzolini, Giampaolo [1 ]
机构
[1] Politecn Milan, Dipartimento Energia, Via Raffaele Lambruschini 4, I-20156 Milan, Italy
[2] Univ Brescia, Dept Mech & Ind Engn, Via Branze 38, I-25123 Brescia, Italy
关键词
CSP; Solar tower plants; Carbon dioxide; Dinitrogen tetroxide; Working fluids; Mixtures of fluids; Supercritical thermodynamic cycles; GAS BRAYTON CYCLES; THERMAL-STABILITY; EQUILIBRIUM; GENERATION; NITROGEN; SODIUM;
D O I
10.1016/j.solener.2019.01.079
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
The competitiveness of concentrated solar power technology in the near-future electricity generation scenario, requires a substantial reduction of the Levelized Cost of Energy which can be achieved with an increase of the energy conversion efficiencies while maintaining or reducing the investment costs. This paper discusses the use of pure Dinitrogen tetroxide N2O4, and N2O4/CO2 mixture, as working fluids in supercritical Brayton cycles applied to solar tower power plants. When N2O4 is combined with CO2, the resulting mixture has a comparatively higher critical temperature than pure CO2, allowing a condensing cycle even at the fairly high ambient temperatures of desert areas, where solar power plants are typically installed. This allows the adoption of simpler cycle configurations than the one used in sCO(2) cycles (cost reduction) while achieving very high thermodynamic efficiency (47% at 700 degrees C). The N2O4/CO2 mixture with optimized composition, integrated in a solar tower unit, increases the solar-electric efficiency by 1% with respect to commercial plants based on steam cycle with 550 degrees C maximum temperature (22.3% vs. 21.3%). At 700 degrees C, the overall solar-electric efficiency can reach 24.5% which is slightly higher than supercritical CO2 cycles, yet with a foreseeable reduction of the investment costs as consequence of the simpler plant lay-out.
引用
收藏
页码:203 / 213
页数:11
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