2016
DOI: 10.1007/s12206-016-1047-z
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Experimental and numerical studies on pressure drop in reverse electrodialysis: Effect of unit cell configuration

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Cited by 5 publications
(7 citation statements)
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“…Moreover, the compartments were asymmetric, because the viscosity of the concentrated solution (brine) was almost twice that of the dilute feed, thus causing an unbalanced pressure distribution in the two solutions. Larger TMP values (up to ~1.5 bar) were measured by Hong et al [27] in a cross-flow RED stack (35.5 × 35.5 cm 2 ) fed with inlet velocities up to ~5 cm/s, which provided a significantly lower electrical power (less than half) compared to an equivalent parallel-flow stack. Although the authors attributed this decline in performance to issues of internal leakage, an important effect of deformation can be supposed.…”
Section: Introductionmentioning
confidence: 92%
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“…Moreover, the compartments were asymmetric, because the viscosity of the concentrated solution (brine) was almost twice that of the dilute feed, thus causing an unbalanced pressure distribution in the two solutions. Larger TMP values (up to ~1.5 bar) were measured by Hong et al [27] in a cross-flow RED stack (35.5 × 35.5 cm 2 ) fed with inlet velocities up to ~5 cm/s, which provided a significantly lower electrical power (less than half) compared to an equivalent parallel-flow stack. Although the authors attributed this decline in performance to issues of internal leakage, an important effect of deformation can be supposed.…”
Section: Introductionmentioning
confidence: 92%
“…However, in prototype and industrial size stacks with non-parallel flow layouts (cross flow, counter flow) and/or with asymmetric channels (different geometries, fluid properties, flow rates), where the pressure distribution in the two compartments is different, appreciable values of TMP may arise. In particular, when some factors enhancing pressure drop are present, TMP values amounting to some tenths of a bar can be exhibited (higher TMP levels can cause severe risks of leakages [25,26,27]).…”
Section: Introductionmentioning
confidence: 99%
“…The manifolds geometry, along with the channel features and the operating conditions (flow rate and relative direction of the concentrate and diluate streams), also affect the distribution of flow rates (and thus of pressure) among the compartments and in each compartment, with consequences on non-Ohmic resistances, solution leakages from the concentrate channel towards the dilute one and vice versa, and fouling [260,318,[320][321][322][323]. The increase of non-Ohmic resistance arising from a nonuniform distribution of the flow rate can be explained by the exponential reduction of the non-Ohmic resistance with the flow rate.…”
Section: Inlet-outlet Manifolds In Plate and Frame Unitsmentioning
confidence: 99%
“…In this respect, wider manifolds lead to a more uniform delivery of feed solutions flow rate, with beneficial effects in terms of non-Ohmic resistances reduction [260]. Finally, large differential pressures between adjacent compartments cause solution leakages through the membrane [322], occurring especially in counter-current and cross-flow configurations [321].…”
Section: Inlet-outlet Manifolds In Plate and Frame Unitsmentioning
confidence: 99%
“…However, many membrane processes, including ED and RED, may experience membrane deformation due to a transmembrane pressure (TMP) between fluid channels [14][15][16][17][18][19][20]. For example, Hong et al [21] performed experimental and numerical studies of an RED stack with 200 cell pairs, showing a high pressure difference between seawater and fresh water channels.…”
Section: Motivation and Strategy Of The Present Studymentioning
confidence: 99%