Sensitivity of transcritical cycle and turbine design to dopant fraction in CO2-based working fluids

被引:19
作者
Aqel, O. A. [1 ]
White, M. T. [1 ]
Khader, M. A. [1 ]
Sayma, A., I [1 ]
机构
[1] City Univ London, Dept Mech Engn & Aeronaut, Northampton Sq, London EC1V 0HB, England
基金
欧盟地平线“2020”;
关键词
Transcritical Rankine cycle; Axial turbine; Sensitivity analysis; CSP; CO2-based mixtures; Dry-cooling; ORGANIC RANKINE-CYCLE; CARBON-DIOXIDE; SUPERCRITICAL CO2; BRAYTON CYCLES; SOLAR TOWER; POWER; MIXTURES; ORC; ENERGY; HEAT;
D O I
10.1016/j.applthermaleng.2021.116796
中图分类号
O414.1 [热力学];
学科分类号
摘要
Supercritical CO2 (sCO(2)) power cycles have gained prominence for their expected excellent performance and compactness. Among their benefits, they may potentially reduce the cost of Concentrated Solar Power (CSP) plants. Because the critical temperature of CO2 is close to ambient temperatures in areas with good solar irradiation, dry cooling may penalise the efficiency of sCO(2) power cycles in CSP plants. Recent research has investigated doping CO2 with different materials to increase its critical temperature, enhance its thermodynamic cycle performance, and adapt it to dry cooling in arid climates. This paper investigates the use of CO2/TiCl4, CO2/NOD (an unnamed Non-Organic Dopant), and CO2/C6F6 mixtures as working fluids in a transcritical Rankine cycle implemented in a 100 MWe power plant. Specific focus is given to the effect of dopant type and fraction on optimal cycle operating conditions and on key parameters that influence the expansion process. Thermodynamic modelling of a simple recuperated cycle is employed to identify the optimal turbine pressure ratio and recuperator effectiveness that achieve the highest cycle efficiency for each assumed dopant molar fraction. A turbine design model is then used to define the turbine geometry based on optimal cycle conditions. It was found that doping CO2 with any of the three dopants (TiCl4, NOD, or C6F6) increases the cycle's thermal efficiency. The greatest increase in efficiency is achieved with TiCl4 (up to 49.5%). The specific work, on the other hand, decreases with TiCl4 and C6F6, but increases with NOD. Moreover, unlike the other two dopants, NOD does not alleviate recuperator irreversibility. In terms of turbine design sensitivity, the addition of any of the three dopants increases the pressure ratio, temperature ratio, and expansion ratios across the turbine. The fluid's density at turbine inlet increases with all dopants as well. Conversely, the speed of sound at turbine inlet decreases with all dopants, yet higher Mach numbers are expected in CO2/C6F6 turbines.
引用
收藏
页数:17
相关论文
共 38 条
[1]  
Allison TC, 2017, WOODHEAD PUBL SER EN, P147, DOI 10.1016/B978-0-08-100804-1.00007-4
[2]   Energy and exergy analyses of solar tower power plant driven supercritical carbon dioxide recompression cycles for six different locations [J].
Atif, Maimoon ;
Al-Sulaiman, Fahad A. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2017, 68 :153-167
[3]   Dinitrogen tetroxide and carbon dioxide mixtures as working fluids in solar tower plants [J].
Binotti, Marco ;
Invernizzi, Costante M. ;
Iora, Paolo ;
Manzolini, Giampaolo .
SOLAR ENERGY, 2019, 181 :203-213
[4]   CO2-TiCl4 working fluid for high-temperature heat source power cycles and solar application [J].
Bonalumi, D. ;
Lasala, S. ;
Macchi, E. .
RENEWABLE ENERGY, 2020, 147 :2842-2854
[5]   Energetic optimization of regenerative Organic Rankine Cycle (ORC) configurations [J].
Braimakis, Konstantinos ;
Karellas, Sotirios .
ENERGY CONVERSION AND MANAGEMENT, 2018, 159 :353-370
[6]   Supercritical carbon dioxide cycles for power generation: A review [J].
Crespi, Francesco ;
Gavagnin, Giacomo ;
Sanchez, David ;
Martinez, Gonzalo S. .
APPLIED ENERGY, 2017, 195 :152-183
[7]   Vapor-liquid equilibrium of carbon dioxide-perfluoroalkane mixtures:: Experimental data and SAFT modeling [J].
Dias, AMA ;
Carrier, H ;
Daridon, JL ;
Pàmies, JC ;
Vega, LF ;
Coutinho, JAP ;
Marrucho, IM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (07) :2341-2350
[8]  
Dixon C.H.S.L., 2014, FLUID MECH THERMODYN, Vseventh, P556
[9]  
Dostal V., 2004, Report No.: MIT-ANP-TR-100
[10]   Economic analysis of Organic Rankine Cycle (ORC) and Organic Rankine Cycle with internal heat exchanger (IORC) based on industrial waste heat source constraint [J].
Fan Wei ;
Guo Senchuang ;
Han Zhonghe .
INNOVATIVE SOLUTIONS FOR ENERGY TRANSITIONS, 2019, 158 :2403-2408