2020
DOI: 10.1016/j.memsci.2020.117889
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Optimization of two-stage seawater reverse osmosis membrane processes with practical design aspects for improving energy efficiency

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Cited by 27 publications
(11 citation statements)
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“…The solution-diffusion model was primarily used for the description of the water purification [30,33,36,38,47,50,64,65], including sea water [25,40,41,43,49,52,55,57,61,66] and brackish water [20,31,42,45,58,59,60,65] desalination, and also the wastewater treatment [30, 48, 51, 53-54, 56, 67]. Also, with using of this model it was described the processes of the removal of zinc [32], boron [28,52], chlorophenol [36,38], N-nitrosodimethylamine [38,63], weak acids [25], and ammonia compounds [51,54], apple juice concentration [35,37], and also for the membrane characterization [46].…”
Section: F11mentioning
confidence: 99%
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“…The solution-diffusion model was primarily used for the description of the water purification [30,33,36,38,47,50,64,65], including sea water [25,40,41,43,49,52,55,57,61,66] and brackish water [20,31,42,45,58,59,60,65] desalination, and also the wastewater treatment [30, 48, 51, 53-54, 56, 67]. Also, with using of this model it was described the processes of the removal of zinc [32], boron [28,52], chlorophenol [36,38], N-nitrosodimethylamine [38,63], weak acids [25], and ammonia compounds [51,54], apple juice concentration [35,37], and also for the membrane characterization [46].…”
Section: F11mentioning
confidence: 99%
“…The important factor of the successive optimization procedure includes the choice of the target function and the optimization criterion. As in 20200-2010, in the considered period in most works authors used the economical optimization criteria, primarily the minimization of costs [49,61,[74][75][202][203][204][205][206][207][208][209][210][211][212][213][214][215][216][217], and also the minimization of the energy consumption, which is the significant part of the operational cost [27,38,49,66,73,[204][205][219][220][221][222][223][224][225][226][227][228]. Also, the economic criteria included the profit maximization [229][230], and the minimization of the cost factor, which in work [231] was determined as the ratio of the water price and energy price in a hybrid system with reverse osmosis and pressure retarded osmosis.…”
Section: Optimization and Process Controlmentioning
confidence: 99%
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“…Kim et al modeled the practical design of a 100 000 m 3 day −1 two‐stage SWRO to improve the energy efficiency under various operating conditions. [ 137 ] With the same number of membrane modules, both single‐ and two‐stage SWRO offered similar permeate quality but the latter always exhibited greater energy consumption for a given recovery rate. The optimal ratio of the number of pressure vessels for the first stage to the second was determined as the function of ERD type.…”
Section: Strategies For Energy Reduction In Desalination Processesmentioning
confidence: 99%
“…Numerous publications have researched the optimisation of brackish water reverse osmosis (BWRO) (5000–15,000 mg/L TDS) [ 4 , 5 , 6 , 7 , 8 ] and salt water reverse osmosis (SWRO) (15,000 mg/L–35,000 mg/L) [ 4 , 5 , 9 , 10 , 11 ]. However, it is much less energy-intensive to perform reverse osmosis on low salinity water between 500 and 5000 mg/L as there is less osmotic pressure to overcome.…”
Section: Introductionmentioning
confidence: 99%