Optimizing the energy recovery section in thermal desalination systems for improved thermodynamic, economic, and environmental performance

被引:30
作者
Jamil, Muhammad Ahmad [1 ,2 ]
Goraya, Talha S. [2 ]
Ng, Kim Choon [3 ]
Zubair, Syed M. [4 ]
Xu, Ben Bin [1 ]
Shahzad, Muhammad Wakil [1 ,3 ]
机构
[1] Northumbria Univ, Mech & Construct Engn Dept, Newcastle Upon Tyne NE1 8ST, Tyne & Wear, England
[2] Khwaja Fareed Univ Engn & Informat Technol, Dept Mech Engn, Rahim Yar Khan, Pakistan
[3] King Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 239556900, Saudi Arabia
[4] King Fahd Univ Petr & Minerals, Mech Engn Dept, Box 1474, Dhahran 31261, Saudi Arabia
基金
英国工程与自然科学研究理事会;
关键词
Plate heat exchangers; Preheaters; Desalination; Energy recovery; Genetic algorithm; Optimization; Economic analysis; PLATE HEAT-EXCHANGER; SHELL-AND-TUBE; MULTI EFFECT DESALINATION; THERMOECONOMIC ANALYSIS; THERMOPHYSICAL PROPERTIES; EFFECT EVAPORATION; OPTIMAL-DESIGN; PRESSURE-DROP; PUMP SYSTEM; OPTIMIZATION;
D O I
10.1016/j.icheatmasstransfer.2021.105244
中图分类号
O414.1 [热力学];
学科分类号
摘要
Integration of energy recovery section with thermal desalination systems improves their performance from thermodynamics, economics, and environmental viewpoints. This is because it significantly reduces input energy, heat transfer area, and capital cost requirements. Above all, the system outlet streams can achieve thermal equilibrium with the environment by supplying heat for useful preheating purposes thus reducing the environmental impacts. The plate heat exchangers are generally employed for this purpose as preheaters. The current paper presents a comprehensive investigation and optimization of these heat exchangers for thermal desalination systems applications. An experimentally validated numerical model employing Normalized Sensitivity Analysis and Genetic Algorithm based cost optimization is developed to investigate their performance at assorted operating conditions. The analysis showed that the heat transfer coefficient, pressure drop, and outlet water cost were improved by an increase in feed flow rate. However, with an increased flow rate, the comprehensive output parameter (h/Delta P) decreased due to the high degree increase in pressure drop. Moreover, an increase in the chevron angle reduced the heat transfer coefficient, pressure drop, and water cost. Finally, the optimization lowered the heat transfer area by similar to 79.5%, capital investment by similar to 62%, and the outlet cost of the cold stream by similar to 15.7%. The operational cost is increased due to the increased pressure drop but the overall impact is beneficial as C-total of equipment is reduced by similar to 52.7%.
引用
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页数:12
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