Thermo-Economic Optimization of an Idealized Solar Tower Power Plant Combined with MED System

Based on the reversible heat engine model, theoretical analysis is carried out for economic performance of a solar tower power plant (STPP) combined with multi-effect desalination (MED). Taking total revenue of the output power and the fresh water yield per unit investment cost as the economic objective function, the most economical working condition of the system is given by analyzing the influence of the system investment composition, the receiver operating temperature, the concentration ratio, the efficiency of the endoreversible heat engine, and the relative water price on the economic parameters of the system. The variation curves of the economic objective function are given out when the main parameter is changed. The results show that the ratio of water price to electricity price, or relative price index, has a significant impact on system economy. When the water price is relatively low, with the effect numbers of the desalination system increasing, and the economic efficiency of the overall system worsens. Only when the price of fresh water rises to a certain value does it make sense to increase the effect. Additionally, the threshold of the fresh water price to the electricity price ratio is 0.22. Under the conditions of the current price index and the heliostat (or reflector), the cost ratio and the system economy can be maximized by selecting the optimum receiver temperature, the endoreversible heat engine efficiency, and the optimum concentration ratio. Given the receiver surface temperature and the endoreversible heat engine efficiency, increasing the system concentration ratio of the heliostat will be in favor of the system economy.

[1]  Hans Müller-Steinhagen,et al.  Technologies for large scale seawater desalination using concentrated solar radiation. , 2009 .

[2]  Ronan K. McGovern,et al.  Optimal concentration and temperatures of solar thermal power plants , 2012 .

[3]  Bartolomé Ortega-Delgado,et al.  Thermoeconomic comparison of integrating seawater desalination processes in a concentrating solar power plant of 5 MWe , 2016 .

[4]  Yuehong Su,et al.  Thermodynamic analysis of an idealised solar tower thermal power plant , 2015 .

[5]  Yasin Ust,et al.  Thermoeconomic analysis of a solar driven heat engine , 2006 .

[6]  Guillermo Zaragoza,et al.  Large-scale solar desalination by combination with CSP: Techno-economic analysis of different options for the Mediterranean Sea and the Arabian Gulf , 2015 .

[7]  Germain Augsburger,et al.  Thermoeconomic optimization of a combined-cycle solar tower power plant , 2012 .

[8]  Nidal Abu-Hamdeh,et al.  Design considerations and construction of an experimental prototype of concentrating solar power tower system in Saudi Arabia , 2016 .

[9]  C. Frantz,et al.  Thermal Analysis of a Multi Effect Distillation Plant Powered by a Solar Tower Plant , 2015 .

[10]  Yasin Ust Effects of combined heat transfer on the thermo-economic performance of irreversible solar-driven heat engines , 2007 .

[11]  Q. Yang,et al.  Energy cost and greenhouse gas emissions of a Chinese solar tower power plant , 2011 .

[12]  Marco A. Barranco-Jiménez,et al.  Thermoeconomic Optimum Operation Conditions of a Solar-driven Heat Engine Model , 2009, Entropy.

[13]  Francisco J. Collado,et al.  A review of optimized design layouts for solar power tower plants with campo code , 2013 .

[14]  Stefan Will,et al.  Techno-economic analysis of combined concentrating solar power and desalination plant configurations in Israel and Jordan , 2012 .

[15]  Kun Wang,et al.  Thermodynamic analysis and optimization of a molten salt solar power tower integrated with a recompression supercritical CO2 Brayton cycle based on integrated modeling , 2017 .

[16]  Abdallah Khellaf,et al.  A review of studies on central receiver solar thermal power plants , 2013 .