Optimizing solarized desalination unit through the implementation of 4-step MED method using energy, exergy, economic and environmental analysis

被引:4
作者
Imandoust, Milad [1 ]
Alghorayshi, Seyed Taher Kermani [2 ]
Asadi, Behrang [3 ]
Montazeri, Ali [4 ]
Moradi, Farshad [1 ]
Zahedi, Rahim [5 ]
机构
[1] Iran Univ Sci & Technol, Fac Chem Engn, Dept Chem Engn, Tehran, Iran
[2] Univ Isfahan, Fac Adv Sci & Technol, Dept Renewable Energy Engn, Esfahan, Iran
[3] Univ Tehran, Fac Chem Engn, Dept Chem Engn, Tehran, Iran
[4] Mat & Energy Res Ctr, Dept Renewable Energy Engn, Tehran, Iran
[5] Univ Tehran, Dept Energy Governance, Tehran, Iran
关键词
Renewable cogeneration process; Multi effect distillation; Optimization; Energy & exergy analysis; Life cycle assessment; REVERSE-OSMOSIS DESALINATION; OXIDE FUEL-CELL; GAS-TURBINE; NSGA-II; SOFC-GT; POWER; OPTIMIZATION; SYSTEM; PERFORMANCE; GENERATION;
D O I
10.1016/j.jenvman.2024.122707
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The consumption of thermal energy in thermal desalination plants leads to a higher price for the fresh water they produce compared to other methods. By utilizing optimization techniques, it is possible to lower both energy consumption and price. The focus of this paper is on optimizing a solarized desalination unit through the implementation of the 4-step MED method with a PTC collector. To achieve this objective, the NSGA II algorithm was implemented in MATLAB using a function for optimization. This algorithm is known for its cost-effectiveness and high energy efficiency. According to the results, there has been an improvement in the fresh water flow rate, desalination efficiency, and GOR, with values reaching 126.87, 53.6%, and 3.66 respectively, compared to the previous values of 116.5, 49.21%, and 3.32. In the ideal condition, the power generated is 6089 kW, priced at 3.28 cents per kilowatt, and the cost of producing fresh water is 8.49 dollars per cubic meter, which decreases as the process lifespan increases. Solar collectors and thermal tanks account for the largest portion (64%) of exergy destruction, as indicated by the exergy analysis. Optimization of the process has led to energy and exergy efficiencies of 59.8% and 58%, respectively, representing a notable enhancement of around 10% in the system's lifespan. The optimal mode also includes the completion of the sensitivity analysis. The process was subjected to LCA analysis, and the results indicated that the largest impact is on human health, with the collectors and thermal storage tanks being responsible for most of the pollution. As a result, the optimized process has delivered outstanding results while also being environmentally conscious.
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页数:16
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