2003
DOI: 10.1016/s0011-9164(03)00394-1
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Optimization of energy consumption in the 3300 m3/d RO Kerkennah plant

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Cited by 21 publications
(13 citation statements)
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“…By constraining the effluent concentration in all simulations to the drinking water total dissolved solids standard (500 mg L –1 ), these findings enable a comparison of CDI architecture specific thermodynamic efficiency and volumetric energy consumption to that of RO. When energy recovery was included, mean thermodynamic efficiency (η T* ) for MCDI ranged from 10% to 20% (maximum of 62% under optimal conditions, Table S3), which is greater than the reported range for pilot and full-scale brackish water RO systems (1–16% thermodynamic efficiency assuming dilute concentration of 15 mg L –1 NaCl), , A recent study by Qin et al, in which MCDI was simulated for comparison with RO using a highly simplistic Randle’s circuit, estimated MCDI thermodynamic efficiency between 5% and 10% when comparably operated due to an assumed energy recovery of 33%. Alternatively, the mean simulated round-trip efficiency in this study projects that 54–58% of energy consumed during charging, across all electrode thicknesses and influent concentrations, would be available for recovery in MCDI (Figure and Table S3).…”
Section: Resultsmentioning
confidence: 83%
“…By constraining the effluent concentration in all simulations to the drinking water total dissolved solids standard (500 mg L –1 ), these findings enable a comparison of CDI architecture specific thermodynamic efficiency and volumetric energy consumption to that of RO. When energy recovery was included, mean thermodynamic efficiency (η T* ) for MCDI ranged from 10% to 20% (maximum of 62% under optimal conditions, Table S3), which is greater than the reported range for pilot and full-scale brackish water RO systems (1–16% thermodynamic efficiency assuming dilute concentration of 15 mg L –1 NaCl), , A recent study by Qin et al, in which MCDI was simulated for comparison with RO using a highly simplistic Randle’s circuit, estimated MCDI thermodynamic efficiency between 5% and 10% when comparably operated due to an assumed energy recovery of 33%. Alternatively, the mean simulated round-trip efficiency in this study projects that 54–58% of energy consumed during charging, across all electrode thicknesses and influent concentrations, would be available for recovery in MCDI (Figure and Table S3).…”
Section: Resultsmentioning
confidence: 83%
“…A general industrial RO process is composed of intaking raw water, a pretreatment step, the RO system, a posttreatment step, and water supply pumping [5,10,[22][23][24][25][26][27][28][29]. The pretreatment step includes sieves, chlorination, coagulation, flocculation, sedimentation, multimedia filtration, cartridge filtration, de-chlorination, and adding acid or anti-scalant [23].…”
Section: Introductionmentioning
confidence: 99%
“…The RO system is composed of a highpressure pump, RO modules, and an energy recovery device (ERD) [23]. The post-treatment step includes degassing, remineralization, neutralization and disinfection [5,10,[22][23][24][25][26][27][28][29][30].…”
Section: Introductionmentioning
confidence: 99%
“…Published research on SWRO has investigated reducing the SEC by optimising the membrane module [2,[5][6][7][8][9][10][11][12][13] and/or using more permeable membranes [8,[14][15][16]. However, these studies have utilised modelling tools [1,2] without process simulation tools.…”
Section: Introductionmentioning
confidence: 99%