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Cited by 11 publications
(7 citation statements)
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“…Table 2 summarizes exergy efficiency for some of the standalone and integrated processes. In contrast to MD, the majority of the exergy rates in RO are derived from the high pressures involved, i.e., 15-25 bars for brackish water and 60-80 bars for seawater, hence the related pressure drop as reflected in improved efficiencies when a pressure exchanger is considered [19]. The very low exergy efficiency of MD reported [4] was from the one powered by solar, and the high exergy losses were due to the MD and heat exchanger units.…”
Section: Exergy Efficiency Of the Agmd Modulesmentioning
confidence: 99%
“…Table 2 summarizes exergy efficiency for some of the standalone and integrated processes. In contrast to MD, the majority of the exergy rates in RO are derived from the high pressures involved, i.e., 15-25 bars for brackish water and 60-80 bars for seawater, hence the related pressure drop as reflected in improved efficiencies when a pressure exchanger is considered [19]. The very low exergy efficiency of MD reported [4] was from the one powered by solar, and the high exergy losses were due to the MD and heat exchanger units.…”
Section: Exergy Efficiency Of the Agmd Modulesmentioning
confidence: 99%
“…The chemical exergy of a material stream is the amount of exergy transferred over a chemical reaction at the ambient pressure and temperature until the chemical equilibrium is achieved. The specific molar chemical exergy ( ex ch ) of ideal gas mixtures or ideal liquids can be obtained using eq , as given below: …”
Section: Methodsmentioning
confidence: 99%
“…For nonideal liquids, it is preferred to calculate specific molar chemical exergy using eq where ex ch, i 0 , M i , and γ i introduce the standard molar chemical exergy, the molarity, and the molar activity of component i in the liquid mixture, respectively.…”
Section: Methodsmentioning
confidence: 99%
“…Mixing exergy is always a negative value because the mixing of different components decreases the exergy continuously along the length of the reactor [ 28 ]. It can also be written in the form of , where P i is the partial pressure of each component ( P i = χ i P total ) according to Dalton’s law [ 32 ].…”
Section: Process and Exergymentioning
confidence: 99%