2012
DOI: 10.1016/j.desal.2012.06.003
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Remineralization of Reverse Osmosis (RO)-desalted water for a Moroccan desalination plant: optimization and cost evaluation of the lime saturator post

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Cited by 28 publications
(12 citation statements)
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“…The operating costs of the WWRPs and SWDPs consist of the costs of overheads, energy, chemicals, consumables, and spare parts, and are presumed as $0.35–0.85/m 3 for the WWRPs, and $0.5–1.1/m 3 for the SWDPs [ Karagiannis and Soldatos , ; Reddy and Ghaffour , ]. Also included in the costs is the cost of posttreatment of the desalinated water (i.e., lime addition for pH adjustment [ El Azhar et al ., ], remineralization [ Rygaard et al ., ], and chlorine disinfection) amounting to $0.1/m 3 .…”
Section: Methods and Datamentioning
confidence: 99%
“…The operating costs of the WWRPs and SWDPs consist of the costs of overheads, energy, chemicals, consumables, and spare parts, and are presumed as $0.35–0.85/m 3 for the WWRPs, and $0.5–1.1/m 3 for the SWDPs [ Karagiannis and Soldatos , ; Reddy and Ghaffour , ]. Also included in the costs is the cost of posttreatment of the desalinated water (i.e., lime addition for pH adjustment [ El Azhar et al ., ], remineralization [ Rygaard et al ., ], and chlorine disinfection) amounting to $0.1/m 3 .…”
Section: Methods and Datamentioning
confidence: 99%
“…The permeate of the RO unit is not directly potable due its low alkalinity and must be remineralised with hardening components (Ca 2þ and Mg 2þ ). The model follows the remineralisation process described by (El Azhar et al 2012), to reach a total hardness higher than 1 mmol/L required to meet Dutch potable water quality legislation (Beyer et al 2014). Considering the low solubility of lime in water this process applies a lime saturation tank and a mixer that feeds an adequate amount of lime saturated water into the RO permeate (El Azhar et al 2012).…”
Section: Modelled Matps and Process Design Choicesmentioning
confidence: 99%
“…The model follows the remineralisation process described by (El Azhar et al 2012), to reach a total hardness higher than 1 mmol/L required to meet Dutch potable water quality legislation (Beyer et al 2014). Considering the low solubility of lime in water this process applies a lime saturation tank and a mixer that feeds an adequate amount of lime saturated water into the RO permeate (El Azhar et al 2012). Remineralisation of water after reverse osmosis can improve drinking water quality significantly and even allows the adjustment of total dissolved solid contents to empirically confirmed concentrations that provide users with the most favourable taste intensity (Vingerhoeds et al 2016).…”
Section: Modelled Matps and Process Design Choicesmentioning
confidence: 99%
“…DOI: 10.24850/j-tyca-2020-03-08 alimentación, produciendo un agua no estable que puede causar problemas en la salud de la población que la bebe. Además, el agua osmotizada genera problemas de corrosión en las tuberías y/o estructuras auxiliares en los sistemas de distribución (Biyoune et al, 2017;Liang et al, 2013a;El-Azhar et al, 2012), por lo cual es indispensable contar con sistemas de postratamiento.…”
Section: Introductionunclassified