2010
DOI: 10.1016/j.desal.2010.03.032
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Optimal model for multi effect desalination system integrated with gas turbine

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Cited by 38 publications
(16 citation statements)
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“…-Integration of TDPs as bottoming units of a power generation system, into a "dual purpose" or "cogeneration of electricity and water" configuration that can be either used for large-scale plants like combined cycles or gas turbines [4] or in small-to mediumscale plants including reciprocate engines [5] or micro-turbines. In such configurations the high grade (i.e.…”
Section: Introductionmentioning
confidence: 99%
“…-Integration of TDPs as bottoming units of a power generation system, into a "dual purpose" or "cogeneration of electricity and water" configuration that can be either used for large-scale plants like combined cycles or gas turbines [4] or in small-to mediumscale plants including reciprocate engines [5] or micro-turbines. In such configurations the high grade (i.e.…”
Section: Introductionmentioning
confidence: 99%
“…On the basis of energy consumption and heat transfer, it has been found that MED was more efficient than MSF [11]. The significant advantages, including low scale formation, easy operation, high performance ratio (PR), and operating with any available source of heat energy, have made MED to be widely used in seawater desalination [12][13][14]. For example, 14.5% of desalination plants adopt MED in China and the overall desalination capacity of MED is 232,000 m 3 /d [15][16][17].…”
Section: Desalination and Water Treatmentmentioning
confidence: 98%
“…Water product (d6 in Figure 3) and concentrated seawater (B6 in Figure 3) are then pumped out from the last stage of the evaporator. 16 Figure 3 shows a METVC unit for which the following assumptions are used: 5,12,14
Figure 3.A METVC unit. METVC: multi-effect thermal vapour compression.
All processes are steady state steady flow, neglecting effects of kinetic and potential energy The product leaving any stage is salt free To achieve the optimum operating condition, the temperature difference between effects are assumed to be equal The brine surface effect in flash evaporation in evaporators is neglected The maximum achievable concentration of the rejected brine is 70,000 ppm The mass balance for the entire process is as follows 10 …”
Section: Energy Analysismentioning
confidence: 99%