2021
DOI: 10.1016/j.watres.2021.117498
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Scale-up and Modelling of Flow-electrode CDI Using Tubular Electrodes

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Cited by 27 publications
(18 citation statements)
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“…For example, Nordstrand et al recently designed a parallel arrangement of cells with symmetrically distributed flows to maintain a low pressure drop across the system . Another challenge during scale up of CDI is to make the process continuous, which has been the focus of FCDI ,,, and multichannel MCDI ,,, systems. The latter enables continuous production of both fresh and brine streams by periodically switching the products of the middle and side channels .…”
Section: Performance Comparisons and Process Intensificationmentioning
confidence: 99%
See 1 more Smart Citation
“…For example, Nordstrand et al recently designed a parallel arrangement of cells with symmetrically distributed flows to maintain a low pressure drop across the system . Another challenge during scale up of CDI is to make the process continuous, which has been the focus of FCDI ,,, and multichannel MCDI ,,, systems. The latter enables continuous production of both fresh and brine streams by periodically switching the products of the middle and side channels .…”
Section: Performance Comparisons and Process Intensificationmentioning
confidence: 99%
“…Technoeconomic analyses of CDI also show the importance of achieving long system lifetimes, as capital costs (e.g., electrodes, membranes, frames, current collectors) are expected to outweigh operating costs (e.g., electricity, materials, labor). ,, In particular, it is necessary to understand and mitigate electrode degradation , (see section ) and cell fouling (see section ). Several other publications on CDI optimization and pilot systems provide additional design rules and principles for scale up. ,,,,,,, …”
Section: Performance Comparisons and Process Intensificationmentioning
confidence: 99%
“…In CDI, a detailed interplay between desalination adsorption rate and migration of ions determines the efficiency of ion removal. , Thus, while some modeling work is zero-dimensional (0D), others use one-dimensional (1D) spatial resolution across the thickness of a CDI device, ,, 1D along the length, partial two-dimensional (2D), or full 2D. , Some recent work even introduced simplified three-dimensional (3D) simulations for CDI and coupled 3D steady-state simulations of flow-electrode CDI . Such spatial simulations could identify concentration shocks, local dead zones in the device, flux distributions in new structures, etc. However, the complex interconnected processes in CDI can make modeling unsteady, which limits the detail and applicability of coupled spatiotemporal simulations in higher dimensions.…”
Section: Introductionmentioning
confidence: 99%
“…The velocity of flow electrodes at corners is less than that at straight lines, resulting in the poor consistency of the desalination performance in whole flow channels. Ma et al developed a novel FCDI system consisting tubular electrodes in a shell and tube heat exchanger configuration, which promoted the flow uniformity of carbon slurry in the tubular flow channel and achieved a high desalination performance of 0.15 mg s –1 at 1.2 V . This work inspires us to pay more attention to the flow channel structure for the improvement of the desalination performance in FCDI devices.…”
Section: Introductionmentioning
confidence: 99%