Optimal design of a hybrid thermal- and membrane-based desalination unit based on renewable geothermal energy

被引:15
|
作者
Mohammadi, Mohammad Hadi [2 ]
Abbasi, Hamid Reza [1 ,2 ]
Ghodrat, Maryam [3 ]
机构
[1] Univ Manchester, Dept Chem Engn & Analyt Sci, Manchester, Lancs, England
[2] Iran Univ Sci & Technol, Sch Mech Engn, Tehran, Iran
[3] Univ New South Wales Canberra, Sch Engn & Informat Technol, Canberra, ACT 2610, Australia
关键词
Humidification-dehumidification; Desalination; Geothermal energy; Exergoeconomic analysis; Reverse osmosis; HUMIDIFICATION-DEHUMIDIFICATION DESALINATION; THERMOELECTRIC GENERATOR; MULTIGENERATION SYSTEM; PERFORMANCE ASSESSMENT; WATER DESALINATION; OSMOSIS; DRIVEN; DISTILLATION; OPTIMIZATION; CYCLE;
D O I
10.1016/j.ecmx.2021.100124
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this article, exergoeconomic analysis of a hybrid desalination system driven by renewable geothermal energy source is investigated. Freshwater and electrical power are the products of this system. Humidification - dehumidification (HDH) unit works in parallel with reverse osmosis (RO) unit to produce freshwater and Kalina cycle is the power generator unit. Thermoelectric generator (TEG) is responsible for providing the energy required by RO unit. As both HDH and TEG can operate with low-grade energy, two different modes are suggested for the proposed system. In the first mode, the geothermal low grade energy stream is passed to TEG unit, while in the second, it goes through the HDH unit. The effect of different parameters on four main objective functions is examined in parametric study. Moreover, with the aid of selection maps, the objectives of modes can be compared in different operating conditions. The maximum attainable exergy efficiency is calculated to be 28.86% for mode 2. Single objective optimization studies revealed that the first mode produces the largest amount of freshwater at a rate of 22,072 (m(3)/day), while the minimum achievable freshwater cost and total product cost rate can be obtained in the second mode, which is calculated to be 21.94 (c/m3) and 37.19 ($/GJ). Besides, Sankey diagrams for exergy flow and mass flow of saline water are presented to unravel the impact of each sub-system on exergy and salinity.
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页数:18
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