Exergoeconomic optimization of a forward feed multi-effect desalination system with and without energy recovery

被引:30
|
作者
Abid, Asad [1 ]
Jamil, Muhammad Ahmad [1 ,2 ]
Sabah, Noor Us [1 ]
Farooq, Muhammad Umer [1 ]
Yaqoob, Haseeb [1 ,3 ]
Khan, Liaquat Ali [1 ]
Shahzad, Muhammad Wakil [2 ]
机构
[1] Khwaja Fareed Univ Engn & Informat Technol, Dept Mech Engn, Rahim Yar Khan 64200, Pakistan
[2] Northumbria Univ, Mech & Construct Engn Dept, Newcastle Upon Tyne NE1 8ST, Tyne & Wear, England
[3] Univ Sains Malaysia, Sch Mech Engn, Engn Campus, George Town 14300, Malaysia
关键词
Multi-effect desalination; Genetic algorithm; Exergoeconomic analysis; Cost flow method; Optimization; MULTI EFFECT DESALINATION; EXERGO-ECONOMIC ANALYSIS; REVERSE-OSMOSIS; THERMOECONOMIC ANALYSIS; GENETIC ALGORITHM; HEAT-EXCHANGER; PERFORMANCE; DESIGN; DRIVEN; TURBINE;
D O I
10.1016/j.desal.2020.114808
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The escalating freshwater demand is stimulating the researchers to optimize the performance of desalination technologies. The current study presents the exergoeconomic optimization of a forward feed multi-effect desalination (FF-MED) system under two configurations i.e., conventional MED and MED with energy recovery (MED-ER). A detailed numerical model concerning energy, exergy, and a component-based exergoeconomic analysis is employed to estimate the energy consumption, exergy destruction, and water production cost. Thereafter, the FF-MED-ER system is optimized using a Genetic Algorithm for four different objective functions i. e., maximum gain output ratio (GOR), and minimum specific energy consumption (SEC), exergy destruction, and water production cost. The constraint variables included steam temperature, brine salinity, and the last effect brine temperature. The analysis showed that the incorporation of an energy recovery section increased GOR by 17.9% and decreased SEC and water production cost by 14%, and 10.5%, respectively. Moreover, the optimization improved GOR by 9.26%, decreased SEC by 12.86%, exergy destruction by 12.59%, and the water production cost by 8.25% compared to the standard nonoptimal system.
引用
收藏
页数:14
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