Design methodology and multi-objective optimization of small-scale power-water production based on integration of Stirling engine and multi-effect evaporation desalination system

被引:37
作者
Karambasti, Bahram Mahjoob [1 ]
Ghodrat, Maryam [2 ]
Ghorbani, Ghadir [3 ]
Lalbakhsh, Ali [4 ]
Behnia, Masud [5 ]
机构
[1] Univ Guilan, Dept Mech Engn, Fac Engn, Rasht, Iran
[2] Univ New South Wales Canberra, Sch Engn & Informat Technol, Canberra, ACT, Australia
[3] Razi Univ, Dept Mech Engn, Fac Engn, Kermanshah, Iran
[4] Macquarie Univ, Sch Engn, Sydney, NSW, Australia
[5] Macquarie Univ, Macquarie Grad Sch Management, Sydney, NSW 2109, Australia
关键词
Cogeneration of power-water system; Stirling engine; Multi effect desalination (MED); Small scale production; Multi-objective optimization; Decision-making tools; THERMAL VAPOR COMPRESSION; THERMOECONOMIC ANALYSIS; DISTILLATION PLANT; WASTE HEAT; SIMULATION; PERFORMANCE; GENERATION; MODEL; DRIVEN;
D O I
10.1016/j.desal.2021.115542
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
To meet the raising demands for energy and potable water, integration of power plants and desalination systems for large-scale coproduction have been widely used in the world. However, in remote and rural locations with no infrastructures such as power grids, integration of large-scale systems is not financially viable. This paper presents a conceptual design and a methodology based on the GPU-3 Stirling engine in upstream as prime mover, coupled with three configurations of multi-effect evaporation desalination (MED) unit in downstream to address the power-water demands for areas with lower population. A multi-objective optimization technique is employed to find the optimal design parameters of the proposed hybrid system. Three objective functions namely maximizing power and water production and minimizing the cost of products are considered. Decision-making tools are implemented on the optimal points of each configuration to select the optimized configurations for each cogeneration system. The most effective system is then introduced by implementing Analytical Hierarchy Process (AHP) technique. It is found that the final selected system is capable of delivering 2.58 kW of electricity and 19.92 m3 fresh water per day with 2.07 $ center dot hr(-1 )cost of products which can be divided into 0.29 $ center dot kWhr(-1) and 1.6 $ center dot m(3) for power and water, respectively.
引用
收藏
页数:17
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