2020
DOI: 10.1016/j.jwpe.2019.101014
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Flow uneven-distribution and its impact on performances of forward osmosis module

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Cited by 17 publications
(5 citation statements)
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“…The main parameters affecting the FO process are solute concentration in both draw and feed solution, reverse draw solute flux [ 6 , 151 ] and membrane salt rejection [ 112 ]. In terms of hydrodynamics analysis, several studies [ 109 , 110 ] introduced the structural parameter ( S ), which is used to evaluate effect of the porous layer geometry on ICP: where t s , T and ε represent the support layer membrane thickness, diffusive tortuosity and porosity, respectively.…”
Section: Module Performance Metricsmentioning
confidence: 99%
See 1 more Smart Citation
“…The main parameters affecting the FO process are solute concentration in both draw and feed solution, reverse draw solute flux [ 6 , 151 ] and membrane salt rejection [ 112 ]. In terms of hydrodynamics analysis, several studies [ 109 , 110 ] introduced the structural parameter ( S ), which is used to evaluate effect of the porous layer geometry on ICP: where t s , T and ε represent the support layer membrane thickness, diffusive tortuosity and porosity, respectively.…”
Section: Module Performance Metricsmentioning
confidence: 99%
“…SWM modules have been used for industrial applications of seawater RO (SWRO) since the 1960s [ 3 ], and their use has been further extended to nanofiltration (NF) in the early 1980s [ 4 ]. For emerging osmotic membrane processes such as forward osmosis (FO) and pressure retarded osmosis (PRO), the development of SWMs is still at an early stage and is only limited to lab-scale studies [ 5 , 6 , 7 , 8 ]. Although some researchers report that the hollow fibre membrane configuration is more suitable for FO and PRO processes due to its higher packing density, self-mechanical support properties and better flow control on both sides of the membrane (i.e., lumen and outer surface of fibre) [ 9 , 10 ], a large number of studies published over the years have used flat sheet membranes for assessing FO and PRO processes [ 6 , 11 , 12 , 13 , 14 , 15 , 16 , 17 ].…”
Section: Introductionmentioning
confidence: 99%
“…The Δ P s were set at 0.05, 0.10, 0.15 and 0.20 bar, corresponding to crossflow velocity of 0.5, 1.0, 3.9 and 5.5 cm/s, respectively. The range of cross-flow velocity applied in this study is within the one applied in commercial full-scale module [ 34 ]. It is worth noting that the Δ P was—due to set-up limitation—altered by changing the crossflow velocity by changing the rotation speed of the peristaltic pump ( Figure 1 B).…”
Section: Methodsmentioning
confidence: 99%
“…Both experimental and computational fluid dynamics, working at the module scale, demonstrated the need to improve the understanding of process limitations that could be affected both by channel design and pressure balance in FO modules [ 237 , 244 , 245 , 246 , 247 , 248 , 249 , 250 , 251 , 252 ]. Further studies are required with specific focus on the concentration process with regard to practical operation and limitations.…”
Section: Tuning Fo Process To Tackle Current Limitations For Optimmentioning
confidence: 99%