2017
DOI: 10.1016/j.energy.2017.08.053
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Design and analysis of a forward feed multi-effect mechanical vapor compression desalination system: An exergo-economic approach

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Cited by 62 publications
(24 citation statements)
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“…The traditional analysis is majorly focused on evaluating the consequence of both process and geometric variables. However, in recent studies, the combined analysis of fiscal and process variables gained remarkable importance on the exergoeconomic performance [7,24]. The primary reason is that the system operating with different economic variables i.e., interest rate, electricity cost, and intake chemical cost would have different operation cost (OC) with like thermal and hydraulic performance [6,18].…”
Section: Exergoeconomic Analysismentioning
confidence: 99%
See 1 more Smart Citation
“…The traditional analysis is majorly focused on evaluating the consequence of both process and geometric variables. However, in recent studies, the combined analysis of fiscal and process variables gained remarkable importance on the exergoeconomic performance [7,24]. The primary reason is that the system operating with different economic variables i.e., interest rate, electricity cost, and intake chemical cost would have different operation cost (OC) with like thermal and hydraulic performance [6,18].…”
Section: Exergoeconomic Analysismentioning
confidence: 99%
“…Plate heat exchangers (PHXs) are widely used for heat recovery in thermalbased desalination units as a preheater. The plate heat exchanger offers many benefits including narrow temperature control (ΔT ≤ 5°C), easy maintenance and cleaning, margin to accommodate different loads, and high operational reliability [7]. Furthermore, it is significant to indicate that PHXs as preheaters have rarely been examined in thermal-based desalination units from an optimized cost design and analysis viewpoint [8].…”
Section: Introductionmentioning
confidence: 99%
“…In another study, an exergoeconomic analysis of a forward-feed multi-effect mechanical VC desalination system has been performed. The quantities of specific energy consumption, exergy efficiency and cost of production for this analysis are calculated to be between 7.67 and 11.36 kWh/m 3 , 7 and 11% and 0.86-1.19 $/m 3 , respectively (Jamil and Zubair 2017). In this study, the associated cost with each component is presented in Table 11: In 2017, an exergoeconomic evaluation of a CSP plant in combination with a desalination system has been performed.…”
Section: Exergoeconomic Analysismentioning
confidence: 99%
“…Finally, the brine from the last effect is directed to the brine preheater to preheat the intake seawater. The cost balance equation is generalized in terms of the number of evaporators which can vary as j = 2 to N. The governing equations in the general form are given as [82] : …”
Section: A Sample Thermoeconomic Modelmentioning
confidence: 99%